Home

USER'S MANUAL

Contents

1. 4 5 8 Cargo Deck Lines 00 17 38 Alarm Running 108 Cargo Deck Line Group 197 Venting valves 1 2 3 4 x x x pa pa 68 88 S D Line P7 74 gt 100 00 68 88 Deck line 4 P8 93 Pa x 100 00 68 88 Deck line 3 PB 63 Pa gt x 100 00 64777 1 Deck line 2 P6 04 Pa gt 100 00 Gu768 u Deck line 1 P6 04 gt 100 00 d 60 00 68 98 68 98 x x X x 1 119 114 113 112 111 CHT2000 ULCC II REV 1 1 The vessel is equipped with 4 main liquid lines each with dedicated cargo pump Depending of number of shore connections available in each scenario cross connection on the manifold must be selected From the deck manifolds on port or starboard side the cargo can be routed through pipelines and valves to cargo tanks or from cargo tanks to pump room and manifolds CHT2000 VLCC II ws User s Manual Page 4 51 Doc no SO 0603 A 9 January 1997 4 5 9 Cargo Pump Room 00 20 01 Picture Alarm Running 109 Cargo Pump Room Group 198 118 90 09 High Overboard 168 09 116 2
2. 60 00 Sloptank 9 8 E cow 220 68 88 pa 2 ODM Eductor 46 54 216 gt Crude P9 71 S H oil pa pi 168 08 suct suct S P 68 88 p line ine pk pa LEES mH 939 phy 28 03 68 09 214 PE 99 00 8 1 H Da 8 8 mH eH 0 EA 68 08 213 68 08 P1 99 DET Bot line 4 3 Bot line 3 68 88 Slop SWH COW 5 Ballast line X over X over X line line a LE 215 Bot line 2 60 98 89 08 11 Te d 3 P1 86 P1 86 ot line P1 99 P 0 58 a S W suct P1 85 68 88 X over 514 line a o pig 8 08 pa P6 04 Gu777 u 212 pa 89777 3 P8 95 mea 6188 9 Em mH DE P6 04 Kn Gy767 9 pu 9787 8 P8 94 um sep a 1108 08 115 CHT2000 ULCC II REU 1 2 By clicking the 109 button on the Cargo deck line mimic MD108 direct access the Cargo Pump Room MD 109 is obtained An overall view of cargo pump room Showing pump room with pumps valves lines for cargo and ballast handling It also include the eductor stripping pump oil gas separator tanks and oil discharge monitoring ODM control valves From this mimic the pump room routing is performed Each major component as cargo pumps ODM stripping pump eductor have buttons for easy access to next operating level CHT2000 VLCC II ws User s Manual P
3. 68 88 168 08 68 98 58 09 line line 8 line 3 EC c Dag 68 88 G2748 2 68 98 58 08 Hi i line 2 iine 2 line 2 DEL line 2 Dg 68 88 pH line 1 1 89 08 pu ine ine pig Slop SWH COW S M Crude line line suct oil X over X over line line 1 CHT2000 ULCC II REV 1 3 The picture gives an overview of cross over lines stripping pump and eductor in the pump room There are 4 cross over lines The cargo cross over line connects the 4 cargo lines and the stripping line together The sea water cross over line connects port and starboard sea chest to each of the cargo lines or COP The tank cleaning COW cross over line makes it possible to connect any of the cargo lines COP to the tank cleaning COW line small diameter line stripping pump and eductor The slop cross over line connects each of the cargo lines and the stripping line small diameter line to the slop tanks and to port sea discharge via the ODM The stripping pump is of steam driven piston type To start simply open the steam supply valve in addition to necessary valves on the cargo side CHT2000 VLCC II ws User s Manual Page 4 73 Doc no SO 0603 A 9 January 1997 4 9 Modelling of Stripping facilities The Stripping Pump The reciprocating stripping pump is driven by steam I e Steam su
4. 3 1 St rag 3 1 Environmental Requirements 3 2 Power Requirements pp 3 3 FUNCTIONAL DESCRIPTION 4 Li EOI 4 1 Computer S YSEM E 4 4 TEC2000 Instructor SG 4 7 Fault Syste nice 4 27 WIGS 4 27 Computerised Load Master 4 39 Model D eSs eriIpti lRu et onse 4 41 uuu eii 4 43 4 44 Shear 4 45 unu MU NE 4 47 nen E 4 48 EU 4 49 Loading Discharging t Se ten Ee HL Ut ed ud obice a 4 50 Cargo Deck Ru cC 4 51 Cargo Pump 4 52 Carso Bottom 4 53 Cargo Line 4 54 P 4 54 Carso Line S n sua cm 4 55 Carso Line 4 55 Ballast 4 56 Slop Tanks and Discharge Monittor 4 57 Centre Tank 1 2 3 amp 4 Condition 4 58 CHT2000 VLCC II ws User s Manual Page ii Doc no SO 0603 A 9 January 1997 4 5 18 4 5 19 4 5 20 4 5 21 4 5 22 4 5 23 4 5 24 4 5 25 4 5 26 4 6 4 7 4 8 4 8 1 4 8 2
5. 16 Page 0034 M CARGO LINE 3 BOTTOM PIPING 16 Page 0035 M CARGO LINE 3 DECK PIPING 17 Page 0036 M CARGO LINE 3 PUMP MONITOR 17 Page 0037 M CARGO LINE 3 PUMP DESIGN DATA 18 Page 0040 M CARGO LINE 4 VALVES 18 Page 0041 M CARGO LINE 4 PUMP TURBINE 19 Page 0042 M CARGO LINE 4 PUMP BEARING CONTROL 19 Page 0043 M CARGO LINE 4 VACUUM SEPARATOR 20 Page 0044 M CARGO LINE 4 BOTTOM PIPING 20 Page 0045 M CARGO LINE 4 DECK PIPING 21 CHT2000 VLCC II ws Variable List 2 38 2 39 2 40 2 41 2 42 2 43 2 44 2 45 2 46 2 47 2 48 2 49 2 30 2 51 2 52 2 53 2 54 2 55 2 56 2 57 2 58 2 59 2 60 2 61 2 62 2 63 2 64 2 65 2 66 2 67 2 68 2 69 2 70 2 71 2 72 2 73 2 74 2 75 2 76 2 77 2 78 2 79 2 80 2 81 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0046 M Page 0047 M Page 0050 M 0051 Page 0052 M Page 0053 M Page 0054 M Page 0056 M Page 0057 M Page 0060 M Page 0061 M Page 0062 M Page 0064 M Page 0065 M Page 0070 M Page 0071 M Page 0073 M Page 0074 M Page 0080 M
6. 600 sem Lco EE mm i 200 200 400 600 800 CHT2000 ULCC II REV 1 3 The Bending Moments are calculated from the Shear Force distribution The graphic picture will display three different curves The yellow curve shows maximum permitted bending moment in harbour condition The red curve shows the maximum permitted bending moment in seagoing condition The blue curve shows actual bending moment The bending moments Q in each section 0 12 is expressed in Kilotonnesmeter Each value is equipped with an alarm that activates when the limit value is exceeded Positive bending moments represents hogging condition and negative moments represents sagging condition CHT2000 VLCC II ws User s Manual Page 4 47 Doc no SO 0603 A 9 January 1997 4 5 5 Deflection 00 05 40 Picture Alarm Running HD 105 Deflection Group HEEL CONDITION DEADHEIGHT DRAUGHT meter MES ox 20 o 4 Sea Density D 1025 0 1888 ton 180 80 Aft 1 18 51 Sea temp 25 00 X of 86 17 Mid STBO L 18 30 4 2 summer mark Mid PORT L 18 30 85 Fr 1 Fud L 18 03 s d DISPLRCEHENT STRBILITY meter 3 1908 ton 219 35 GM Corr L5 50 trim EM ni GMCM FS R Heel 10 00 ed 10 72 X0 00 DS Rad 14 91 MET L 9 13 L 8 22 1 8 24 9 19 L 8 08 meter L 8 17 L 8 07 L 6 13 L
7. 9 2 12 Page 1400 AG14 HULL SHEAR FORCES 1 1 9 2 13 Page 1500 15 LM HULL BENDING MOMENTS 1 2 10 2 14 Page 1501 AGI5 LM HULL SHEAR FORCES 2 2 10 2 15 Page 1900 AG19 INERT GAS SYSTEM 1 1 11 2 16 Page 2000 AG20 DISCHARGE MONITOR 1 1 11 Page ii CHT2000 VLCC II ws Alarm List 1 1 Page 0200 1 2 Page 0500 Page 0700 Page 0800 Page 0900 Page 1000 Page 1100 Page 1300 Page 1400 Page 1500 Page 1900 Page 2000 Doc no SO 0604 A January 6 1997 DIRECTORY LIST Page 0100 TANK ULLAGE TANK OXYGEN CONTENT Page 0400 TANK INERT GAS PRESSURE 1 page TANK CARGO TEMPERATURE CARGO PUMP 1 SYSTEM CARGO PUMP 2 SYSTEM CARGO PUMP 3 SYSTEM CARGO PUMP 4 SYSTEM BALLAST PUMP SYSTEM HULL BENDING MOMENTS HULL SHEAR FORCES LOAD MASTER INERT GAS SYSTEM OIL DISCHARGE MONITOR CHT2000 VLCC II ws Alarm List 2 pages 1 page 1 page 1 page 1 page 1 page 1 page 1 page 1 page 1 page 2 pages 1 page 1 page H Page I Page 2 Doc no SO 0604 A January 6 1997 This page is intentionally left blank CHT2000 VLCC II ws Alarm List Doc no SO 0604 A January 6 1997 2 VARIABLE LIST PAGES 2 1 Page 0100 AG01 TANK ULLAGE 1 2 000012 m L 0 5 250 TANK measured 000112
8. L 22 0 H 22 0 SHEAR FORCE section 8 LM 06411 L 18 0 H 18 0 SHEAR FORCE section 9 LM L 06412 L 14 0 H 14 0 SHEAR FORCE section 10 LM M P06413 L 12 0 H 12 0 SHEAR FORCE section 11 LM N 06414 L 20 0 H 20 0 SHEAR FORCE section 12 LM O P Q R 5 2 178 Page 0711 LOAD MASTER HULL BENDING MOMENTS A 006420 ktonm L 700 0 H 700 0 BENDING MOMENT section 0 LM 006421 ktonm L 300 0 H 300 0 BENDING MOMENT section 1 LM D 006422 L 350 0 H 350 0 BENDING MOMENT section 2 LM 006423 ktonm L 500 0 H 500 0 BENDING MOMENT section 3 LM F Q06424 ktonm L 700 0 H 700 0 BENDING MOMENT section 4 LM G Q06425 ktonm L 700 0 Hz700 0 BENDING MOMENT section 5 LM H Q06426 ktonm L 700 0 H 700 0 BENDING MOMENT section 6 LM I 006427 ktonm L 700 0 H 700 0 BENDING MOMENT section 7 LM J Q06430 ktonm L 700 0 H 700 0 BENDING MOMENT section 8 LM 006431 ktonm L 500 0 H 500 0 BENDING MOMENT section 9 LM L Q06432 ktonm L 200 0 H 200 0 BENDING MOMENT section 10 LM M Q06433 ktonm L 200 0 H 200 0 BENDING MOMENT section 11 LM N Q06434 ktonm L 700 0 H 700 0 BENDING MOMENT section 12 LM O P Q R S T CHT2000 VLCC II ws Variable List Page 91 N L06440 L06441 L06442 L06443 L06444 L06445 L06446 L06447 L06
9. 85 HEEL TRIM 20 5 TIME SCALE SHIP STATE WEATHER CONDITION ug rea 285 Time fac 21 00 hour Speed V0 00 knot Wind Beauf 20 00 GL 5 Periode 16 34 hour 4 13 1 SOLAR TIME 7 8 16 68 hour GM m gt X0 00 5 Tank press influence X 0 01 Des 1 Monitor PUMPS Monitor BOILER Monitor MANIFOLD Monitor POLLUTION pump mass 13 69 ktonnes boiler steam mass 30 90 tonnes connected 11 63 hour tank overflow oil M 12 tonnes pump energy 7 79 MWh boiler oil mass M7 22 tonnes total flow 6 6843 m3 h manifold spill oil H0 00 tonnes pump cost 2 1502 815 boiler oil cost 2 1444 1US mean flow 6 6846 m h discharge oil mass M0 00 kg fuel prize 2 200 00 ton total mass M 9 13 ktonnes IG dishcarge mass 2699 99 HC discharge mass 1388 6kg CHT2888 ULCC II REV 1 1 Information on the overall cargo handling performance display the Use of energy pump heating Amount of pollution oil spill hydro carbon gas waist Efficiency of operation manifold connection time Economical Studies The computer accumulates the power consumption during cargo handling operations such as loading discharging ballasting crude oil washing etc Power consumption can be measured as Steam consumption in tonnes Oil consumption in tonnes and USD Total energy consumption in MWh CHT2000 VLCC II ws User s Manual Page 4 61 Doc no SO 0603 A 9 January 1997 This feature enables the students to car
10. 30 STEAM BOILER CONTROL DATA 31 STEAM BOILER ENERGY MONITOR 31 INERT GAS GENERATOR 32 INERT GAS GENERATOR 32 BALLAST TANK MAIN VARIABLES 33 BALLAST TANK MISCELLANEOUS 33 CARGO TANK 1 MAIN VARIABLES 34 CARGO TANK CT 1 VALVES pp 34 CARGO TANK CT 1 FLOWS 35 CARGO TANK 1 LEVELS MASSES 35 CARGO TANK CT 1 HEATING 36 CARGO TANK CT 1 MISCELLANEOUS 36 CARGO TANK WT 1 S MAIN VARIABLES 37 CARGO TANK WT 1 S 37 CARGO TANK WT 1 S FLOWS 38 CARGO TANK WT 1 S LEVELS MASSES 38 CARGO TANK WT 1 S 39 CARGO TANK WT 1 S MISCELLANEOUS 39 CARGO TANK WT 1 P MAIN VARIABLES 40 CARGO TANK WT P VALVES 40 CARGO TANK WT P FLOWS 41 CARGO TANK 1 LEVELS MASSES 4 CARGO TANK WT P HEATING 42 CARGO TANK WT 1 P MISCELLANEOUS 42 CARGO TANK CT 2 M
11. 4 TORQUE CONSTANT 2 I 03065 COP4 TORQUE CONSTANT 3 J K L M N O P Q R S T 2 40 Page 0050 M BALLAST WATER LINE VALVES A B V03220 lt 0 1 gt BW SEA CHEST SHUT OFF VALVE C D V03221 lt 0 1 gt BW SEA CHEST LINE SUCTION VALVE E V03223 lt 0 1 gt BW SEA CHEST LINE DISCHARGE VALVE F G V03222 lt 0 1 gt BW BOTTOM LINE SUCTION VALVE V03224 lt 0 1 gt BW BOTTOM LINE DISCHARGE VALVE I J V03225 lt 0 1 gt BW DECK LINE SHUT OFF VALVE K L V03270 0 1 BW DROP LINE VALVE CT2 03271 0 1 BW DROP LINE VALVE WT2S 03272 0 1 BW DROP LINE VALVE WT2P P Q V03273 lt 0 1 gt BW DROP LINE VALVE CT4 V03274 lt 0 1 gt BW DROP LINE VALVE WT5S 03275 lt 0 1 gt BW DROP LINE VALVE WT5P T Page 22 CHT2000 VLCC II ws Variable List 2 41 V03112 V03113 G03114 P03115 P03116 P03122 N03110 N03101 E03120 703121 703107 SUAS ROMO APS V03103 003106 003104 203105 HaAROVOZ 2 42 241 T03242 g Q gt tri V03111 R03240 R03246 X03247 zr C03100 C03256 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0051 M BALLAST WATER LINE PUMP TURBINE m3 h bar bar bar L 0 0 rpm L 0 0 rpm kW 9 L 0 0 m3 h kWh kg H 20 0 BWP DISCHARGE VALVE POS BWP DISCHARGE VALVE POS COMMAND BWP FLOW BWP DISCHAR
12. SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 8808 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0411 M CARGO TANK WT 5 S VALVES 0 1 96 0 1 0 1 0 1 0 1 0 1 WTSS WTSS WTSS WTSS WTSS WTSS WTSS BOTTOM VALVE CNTR BOTTOM VALVE PORT COW SUPPLY VALVE COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List N E N 001541 001540 003264 001517 001543 001544 001533 001534 SUAS BOAO Oe gt 001570 2 2 130 U01510 L01511 L01513 L01514 X01516 M01503 V01502 M01522 M01523 M01524 M01525 M01507 M01506 M01515 D01520 D01521 Z O 2 O Z lt i R 9 Q Z gt CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0412 M CARGO TANK WT 5 S FLOWS m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT5S BOTTOM OUTLET FLOW CNTR SUCTION WT5S BOTTOM OUTLET FLOW PORT SUCTION BW DROP FLOW INTO TANK WTSS WTSS TANK TOP OVERFLOW WTSS COW CLEANING FLOW WTSS SWW CLEANING FLOW WTSS INERT GAS FLOW FROM MAIN LINE WTSS INERT GAS FLOW TO DECK WTSS TOTAL SUCTION BOBBLE FLOW
13. 2 124 001410 101411 101413 101414 X01416 01403 V01402 M01422 M01423 M01424 M01425 M01407 M01406 M01415 D01420 D01421 Z O 2 O Z lt i R r Q m i 9 Q Z gt Page 64 Doc no SO 0604 A January 6 1997 Page 0402 M CARGO TANK CT 4 FLOWS m3 h m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 CT4 CT4 CT4 BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW PORT SUCTION BOTTOM OUTLET FLOW STBD SUCTION BW DROP FLOW INTO TANK CT4 CT4 CT4 CT4 CT4 CT4 CT4 TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0403 M CARGO TANK CT 4 LEVELS MASSES m m m m CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 30806 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 125 0404 M CARGO TANK CT 4 HEATING A B C T01453 degC 1 40 0 1000 CT4 CARGO TEMPERATURE E 1456 CT4 CARGO HEATING STEAM VALVE G0
14. Air flow rate through the P V valve if vacuum CHT2000 VLCC II ws User s Manual Page 4 75 Doc no SO 0603 A 9 January 1997 Hydrocarbon Gas Content The generation of the hydrocarbon gas will be dependent on Amount of crude oil present in the tank Partial pressure of the hydrocarbon gas in the tank Vapour Pressure The total vapour pressure in a tank is modelled according to the universal gas laws The vapour pressure will be dependent on the vapour volume in the tank the mass of vapour and the temperature of the vapour in the tank Vapour Temperature A regular fluctuation in the vapour pressure caused by the temperature fluctuation between day and night is modelled The solar time can be set from the instructor station Vapour Volume The vapour volume will be dependent on the liquid level in the tank Mass of Vapour The mass of vapour will be dependent on Input flow of gas from the IG plant and or the P V valves Output flow of vapour through the P V valves Generation of hydrocarbon gas CHT2000 VLCC II ws User s Manual Page 4 76 Doc no SO 0603 A 9 January 1997 4 9 2 Oil Water Settling The mixture of oil and water in a tank will after a while due to difference in specific gravity lead to a stratification process The content of oil will be on the top while the water will descend to the bottom The stratification of an oil water mixture will then lead to segregation into three kinds
15. 2 5 Page 0600 MA06 WING TANK 6 VALVES Ne 2 6 Page 0700 MAO7 DECK LINE VALVES 2 7 Page 0800 MA08 LOAD LINE VALVES pe 2 8 Page 0900 MA09 BOTTOM LINE VALVES 2 9 1000 MAIO CARGO PUMP 1 2 2 10 Page LOG MA11 CARGO PUMP 3 4 Ne 2 11 Page 1200 MAI2 BALLAST PUMP eins caecitas ht 2 12 Page 1300 MA13 INERT GAS SYSTEM 2 13 Page 1400 MA14 8 Page ii CHT2000 VLCC II ws Malfunction List Doc no SO 0605 A January 6 1997 1 1 Page 0200 Page 0300 Page 0400 Page 0500 Page 0600 Page 0700 Page 0800 Page 0900 Page 1000 Page 1100 Page 1200 Page 1300 Page 1400 CHT2000 VLCC II ws Malfunction List H DIRECTORY LIST Page 0100 CENTRE TANK 1 2 VALVES CENTRE TANK 3 4 VALVES BALLAST TANK VALVES WING TANK 1 2 VALVES WING TANK 4 5 VALVES WING TANK 6 VALVES DECK LINE VALVES LOAD LINE VALVES BOTTOM LINE VALVES CARGO PUMP 1 2 CARGO PUMP 3 4 BALLAST PUMP INERT GAS SYSTEM MISCELLANEOUS Page I Page 2 Doc no SO 0604 A January 6 1997 This page is intentionally left blank CHT2000 VLCC II ws Malfunction List Doc no SO 0605 A January 6 1997 2 VARIABLE LIST PAGES A M0101 0 100 CT 1 bottom valve V0135 leakage B M0102 0 1 bottom v
16. 4 9 4 9 1 4 9 2 4 9 3 4 9 4 5 1 5 1 1 5 1 2 3 2 3 2 1 5 2 2 5 2 3 5 3 5 3 1 5 3 2 5 3 3 5 4 5 4 1 3 4 2 3 4 3 3 4 4 5 4 5 5 4 6 5 4 7 5 4 8 5 4 9 5 4 10 Wing Tank 1 2 4 5 amp 6 Port Condlition 4 58 Wing Tank 1 2 4 5 amp 6 Stb Condition 4 58 Bunkers and Water Bargraph OD dtd ipd e Uns 4 59 Loading Discharge Ballast 4 60 Eccc HER 4 61 hol 4 64 Inert Gas Rn 4 65 Inert Gas 4 66 Cargo Oil Pump 1 2 3 amp 4 and Separator 4 67 MODELLING OF PUMP CHARACTERISTICS 4 69 Pumping e aD ep d n ar 4 70 Oil Gas Separator With Vacuum 4 7 Ballast Water 4 72 Pump Room Cross over Lines Stripping Pump Eductor Tank Cleaning FISa efy 4 73 Modelling of Stripping facilities a 4 74 PING 4 75 UA Water Settling 4 77 Liquid Tank temperature ate 4 78 Modelling of ResIdues E D 4 78 OPERATION OF THE CHT2000 VLCC II WS et 5 1 TEC2000 Graphic WoTKStatig Ne 5 2 NN E pp 5 2 Keyboar
17. N E gt X07020 X07200 X07201 X07202 X07203 X07204 K X07205 L X07206 M X07207 Sh aot eon gt X07211 X07212 X07213 07214 X07215 HunAovoZz Page 94 Doc no SO 0604 A January 6 1997 Page 0901 M SIM CONTROL TRIP STATE SURVEY lt 0 1 gt lt 0 5 gt lt 0 5 gt lt 0 5 gt lt 0 5 gt lt 0 5 gt L 0 0 L 0 0 L 0 0 L 0 0 L 0 0 H 1 0 H 1 0 H 1 0 H 1 0 H 1 0 EMERGENCY RUN trip inhibit COP1 TRIP INDICATION COP2 TRIP INDICATION COP3 TRIP INDICATION COP4 TRIP INDICATION BWP TRIP INDICATION Page 0902 M SIM CONTROL ALARM SYSTEM lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt EMERGENCY trip inhibit ALARM SYSTEM ACTIVE ALARM OK TANK ULLAGE ALARM OK TANK INERT GAS ALARM OK TANK TEMPERATURE ALARM OK HULL SHEAR BENDING ALARM INERT GAS GENERATOR ALARM OK OIL DISCHARGE MONITOR ALARM LOAD MASTER ALARM CARGO PUMP 1 ALARM CARGO PUMP 2 ALARM OK CARGO PUMP 3 ALARM OK CARGO PUMP 4 ALARM BALLAST PUMP CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 CHT2000 VLCC II ws Variable List Page 95
18. Page 0111 M CARGO TANK WT 1 S VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WTIS WTIS WTIS WTIS WTIS WTIS CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 37 2 71 G00241 G00240 000217 000243 000244 m Q m m 2 O gt G00233 G00234 lt G00270 2 72 U00210 L00211 L00213 L00214 X00216 00203 00202 00222 00223 00224 00225 00207 M00206 M00215 D00220 D00221 Q Z O 2 O Z lt i R r Q r 9 Q Z gt Page 38 Doc no SO 0604 A January 6 1997 0112 M CARGO TANK WT 1 S FLOWS m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WTIS WTIS WTIS WTIS WTIS 15 15 15 BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW PORT SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0113 M CARGO TANK WT 1 S LEVELS MASSES m m m m WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL T
19. 003510 m3 h STEAM FLOW TO TANK HEATING R S T P03530 bar STEAM CONDENSER PRESSURE abs Page 30 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 57 Page 0081 M STEAM BOILER CONTROL DATA A 703513 0 1 BOILER ISOLATION D P03511 STEAM PRESS TO CARGO PUMPS AT ISOLA E T03512 degC STEAM TEMP TO CARGO PUMPS AT ISOLA F G V03517 BOILER STEAM LOAD VALVE AT ISOLA H X03526 BOILER FLUE GAS OXY CONTENT AT ISOLA I J 03520 bar BOILER STEAM PRESSURE SET POINT K L 03521 bar BOILER CONTROLLER GAIN M T03522 sec BOILER CONTR INTEGRATION TIME N C03525 BOILER CONTR STEAM FEEDF GAIN O P T03524 degC BOILER SH STEAM TEMP SET POINT Q 03537 lt 0 1 gt BOILER COMBUSTION COEFF O2 INFLUENCE S T 2 58 Page 0082 M STEAM BOILER ENERGY MONITOR A B X03647 lt 0 1 gt BOILER MONITOR RESET COMMAND D E F 03651 tonn TOTAL BOILER OIL MASS H M03650 tonn TOTAL BOILER STEAM MASS I Z03653 US TOTAL BOILER OIL COST J K L 703655 BOILER FUEL OIL PRICE input 703656 ton CURRENT STEAM COST result N O P Q R S E CHT2000 VLCC II ws Variable List Page 31 2 59 V03572 V03573 V03577 G03574 T03575 X03576 R03570 V03571 L03572 T03573 R03540 03541 03542 03543 lt gt 03544 03545 03546 03547 HARHVOZ 2 60 03530 V03531 V0
20. 00524 00525 00507 M00506 M00515 D00520 D00521 2 O 9 O Z lt 2 AST r Q m m 9 Q Z gt CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0212 M CARGO TANK WT 2 S FLOWS m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT2S BOTTOM OUTLET FLOW CNTR SUCTION WT2S BOTTOM OUTLET FLOW PORT SUCTION BW DROP FLOW INTO TANK WT2S WT2S TANK TOP OVERFLOW WT2S COW CLEANING FLOW WT2S SWW CLEANING FLOW WT2S INERT GAS FLOW FROM MAIN LINE WT2S INERT GAS FLOW TO DECK WT2S TOTAL SUCTION BOBBLE FLOW 0213 M CARGO TANK WT 2 S LEVELS MASSES m m m m 96 WT2S TANK ULLAGE even keel WT2S SOUNDING even keel WT2S CLEAN OIL INTERFACE LEVEL WT2S CLEAN WTR INTERFACE LEVEL WT2S OIL CONTENT IN WTR OIL MIXTURE WT2S TOTAL TANK MASS incl residues WT2S TANK VOLUME cap 9283 m3 WT2S CLEAN OIL MASS WT2S DIRTY OIL MASS WT2S DIRTY WATER MASS WT2S CLEAN WATER MASS WT2S HARD RESIDUES WT2S SOFT RESIDUES WT2S DRIP RESIDUES WT2S OIL DENSITY at 15 dgrC WT2S WTR DENSITY at 15 dgrC Page 47 2 91 100553 V00556 G00557 E00560 E00554 E00555 HP RPOMNOZEU ATT mn Q m m 9 Q gt 2 92 Z00572 P00526 X00527 X00530 M00531 ASH m Q a a 2 OQ m gt P00545 00546 P00547 200568 700569 ARANHVOZ Page 48 Doc no SO 0604 A January 6 1997 Page 0214 M CARGO TANK WT 2 S HEATING degC m3 h k
21. 1660 E01654 E01655 HP RPOMNOZEU ATT m Q m m 9 Q Z gt N W o 001672 P01626 X01627 X01630 M01631 m Q m m oO Q Z gt P01645 P01646 P01647 Z01668 Z01669 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0424 M CARGO TANK WT 5 P HEATING degC m3 h kW kW kW L 40 0 H 100 0 WTSP CARGO TEMPERATURE WTSP CARGO HEATING STEAM VALVE WTSP WTSP CARGO HEATING STEAM FLOW HEAT FROM STEAM WT5P HEAT LOSS SEA AIR WTSP HEAT LOSS TO ADJACENT TANKS Page 0425 M CARGO TANK WT 5 P MISCELLANEOUS 0 2 bar L 0 1 L 0 0 H 0 1 H 8 0 kg M01632 kg bar bar bar DEG DEG WTS5P WTSP WTS5P WTSP WTS5P WTSP WTS5P WTS5P WTSP WTS5P WTSP IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 02 02 32 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT Page 71 N E 29 og U01712 L01711 U01710 V01702 V01701 01703 01705 001750 SUAS m Q a m G01767 P01726 X01727 X01730 01753 HAROVOZ N 4 V01736 1735 1764 m Q m g Q gt V01761 L V01762 M V01763 m EO Pee Page 72 Doc no SO 0604 A January 6 1997 Page 0430 M CARGO
22. CHT2000 VLCC II ws User s Manual Residues ton gt 9 0 1 82687 8 59 08 4 88 98 lt gt tot suct bobl 1 88 00 Inert Gas 210 Crude 0il Hashing Sea Water Washing flow to Cargo Survey CHT2000 ULCC II REV 1 4 Page 5 100 5 9 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Crude Oil Washing COW Before departure on a ballast voyage after the complete discharge of cargo sufficient tanks shall have been crude oil washed to permit complance with the draught and trim requirements during all phases of the ballast voyage Account must be taken of the vessel s trading pattern and expected weather conditions Ballast water should not be put into tanks which have not been crude oil washed Before during and after COW operation check lists must be completed and the student should pay particular attention to the following Mixtures of crude oil and water can produce an electrically charged mist during washing The use of dry crude oil is therefore important and before washing begins any tank which is to be used as a source for crude oil washing fluid should be partly discharged to remove any water which has settled out during the voyage The discharge of a layer at least one metre in depth is necessary for this purpose For the same reason if the slop tank is to be used as a source of oil for washing it should first be completely discharged ashore and
23. G02600 G02601 G02610 G02611 G02602 002565 Zr Pt r r Q m oO gt P02573 T02574 X02575 P02603 T02604 X02605 ARAN VOZ Page 16 Doc no SO 0604 A January 6 1997 Page 0033 M CARGO LINE 3 VACUUM SEPARATOR lt 0 1 gt lt 0 1 gt m bar m3 h m3 h m3 h m3 h m3 h m3 h L 1 0 H 5 0 COP3 VACUUM PUMP START COP3 VACUUM PUMP AUTO SWITCH COP3 SEPARATOR LEVEL COP3 SEPARATOR GAS PRESSURE abs COP3 SEPARATOR INLET LIQUID FLOW COP3 SEPARATOR GAS INFLUX COP3 VACUUM PUMP GAS FLOW FLOW FROM BOTTOM LINE 3 FLOW FROM CO SUCTION CROSSOVER FLOW FROM SW SUCTION CROSSOVER COP3 SEPARATOR OIL CONTENT Page 0034 M CARGO LINE 3 BOTTOM PIPING m3 h m3 h m3 h m3 h m3 h m3 h m3 h m3 h m3 h bar degC bar degC FLOW FROM BOTTOM LINE 3 FLOW FROM SW SUCTION CROSSOVER FLOW FROM CO SUCTION CROSSOVER TOTAL FLOW FROM TANK WT 2 S TOTAL FLOW FROM TANK WT 2 P FLOW FROM TANK CT 3 LOAD LINE 3 CROSS FLOW FROM BLIN4 FLOW FROM FORE TANKS FLOW FROM SLOP TANKS PIPE LINE 3 PRESS aft PIPE LINE 2 TEMP aft PIPE LINE 3 OIL CONTENT aft PIPE LINE 3 PRESS fore PIPE LINE 2 TEMP fore PIPE LINE 3 OIL CONTENT fore CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 29 0035 M CARGO LINE 3 DECK PIPING A 602540 m3 h FLOW FROM COP3 TO DECK LINE 602556 m3 h FLOW FROM COP3 TO TC COW CROSSOVER D 002557 m3 h FLOW FRO
24. K L03572 L T03573 ee Aro 2 Oo Z lt 2 16 Z Z T AST R Q m m 9 Q Z gt CHT2000 VLCC II ws Alarm List 03604 kg Nm L 0 0 Doc no SO 0604 A January 6 1997 Page 1900 AG19 INERT GAS SYSTEM 1 1 m L 0 5 H 0 8 bar L 0 0 0 1 L 0 0 7 0 bar L 0 0 H 0 1 90 L 0 0 6 0 m L 0 2 1 5 IG DECK SEAL SW LEVEL IG DECK LINE GAS PRESSURE IG DECK LINE OXY CONTENT IG DISCHARGE LINE PRESSURE IG DISCHARGE LINE OXY CONTENT IG SCRUBBER SW LEVEL degC L 20 0 H 100 0 IGSCRUBBER GAS OUTLET TEMP Page 2000 AG20 OIL DISCHARGE MONITOR 1 1 X03600 ppm L 0 0 15 0 H 20 0 OVERBOARD OIL CONTENT SPECIFIC OIL DISCHARGE Page 11 Doc no SO 0603 A 6 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Appendix C Malfunction List Doc no SO 0605 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 6 January 1997 3 APPENDIX MALFUNCTION LIST CHT2000 VLCC II ws User s Manual Doc no SO 0604 A January 6 1997 TABLE OF CONTENTS Section Page DIRECTOBY LAST 1 1 Page 0100 CENTRE TANK 1 2 VALVES Ne 2 VARIABLE LIST PAGES ee ree 2 1 Page 0200 MA02 CENTRE TANK 3 4 VALVES 2 2 0300 MA03 BALLAST TANK VALVES 2 3 Page 0400 MA04 WING TANK 1 2 VALVES 2 4 Page 0500 05 WING TANK 4 5 VALVES
25. L 705006 TIME FACTOR 0 705007 TIME FACTOR 1 705010 TIME FACTOR 2 P 705011 TIME FACTOR 3 705012 TIME FACTOR 4 2 2 0003 M SEA SHIP STATE 04000 degC SEA WATER TEMPERATURE 004001 kg m3 SEA WATER DENSITY D E V04003 m s WIND SPEED F T05002 hour SOLAR TIME temp influence G H 04005 0 1 SHIP STATE 0 1 at sea I V04004 knots SHIP SPEED COMMAND J V04002 knots SHIP SPEED K L M L04011 DRAFT AFT 104012 m DRAFT FORE L04015 m DRAFT STBD P L04016 m DRAFT PORT Q R L04013 m HULL TRIM S L04014 m HULL HEEL CHT2000 VLCC II ws Variable List Page 3 Doc no SO 0604 A January 6 1997 2 3 0004 M SHORE CONNECTION DATA A 703700 SHORE PLANT 0 discharge 1 load D 02160 lt 0 1 gt MANIFOLD 1 SHORE CONNECTION stbd V02360 lt 0 1 gt MANIFOLD 2 SHORE CONNECTION 804 02560 0 1 MANIFOLD 3 SHORE CONNECTION 804 02760 0 1 MANIFOLD 4 SHORE CONNECTION 8004 H I V02161 0 1 MANIFOLD 1 SHORE CONNECTION port J V02361 0 1 MANIFOLD 2 SHORE CONNECTION port K V02561 0 1 MANIFOLD 3 SHORE CONNECTION port L V02761 0 1 MANIFOLD 4 SHORE CONNECTION port M N P03701 bar DISCHARGE BACK PRESSURE base O P03702 bar DISCHARGE BACK PRESS RISE CONSTANT P P03703 bar LOAD BACK PRESSURE base P03704 LOAD BACK P
26. Obtain written permission to ballast and a dry tank inspection certificate If any of these conditions cannot be met note this in the record and also note the time date and name of representative Page 5 76 5 7 4 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Ballast that is loaded directly into cargo tanks immediately after cargo discharge comes into contact and mingles with the oil that has remained in the tanks The oily dirty ballast must be disposed off prior to arrival at the loading port unless the loading port has suitable reception facilities Clean Ballast Arrival Ballast Unless it is otherwise specified in the Voyage Orders the vessel should arrive load port with clean ballast and also with decanted slops in accordance with LOT Load on Top procedures Clean arrival ballast is normally filled into one or more CT after the dedicated tanks have been cleaned CT 2 and 4 can be ballasted by using the ballast pump and drop lines Any other CT must be ballasted by using the cargo pumps and lines The Clean Ballast tanks can only be deballasted by using the cargo pumps and lines and therefore considerable pump and line flushing must take place before any overboard discharge of ballast can occur These flushings may not be discharged over board or back flushed into the ballast tanks since these tanks have been thoroughly cleaned and must remain clean Pump and line flushing must therefore be transfe
27. Page 0081 M Page 0082 M Page 0083 M Page 0084 M Page 0090 M Page 0091 M Page 0100 M Page 0101 M Page 0102 M Page 0103 M Page 0104 M Page 0105 M Page 0110 M Page 0111 M Page 0112 M Page 0113 M Page 0114 M Page 0115 M Page 0120 M Page 0121 M Page 0122 M Page 0123 M Page 0124 M Page 0125 M Page 0200 M CARGO LINE 4 PUMP MONITOR 21 CARGO LINE 4 PUMP DESIGN DATA 22 BALLAST WATER LINE 22 BALLAST WATER LINE 23 BALLAST WATER LINE PUMP BEARING CONTROL 23 BALLAST WATER LINE FLOWS 24 BALLAST WATER LINE PRESSURES 24 BALLAST WATER LINE PUMP MONITOR PAGE 25 BALLAST WATER LINE PUMP DESIGN DATA 25 CROSS OVER LINES 26 STRIPPING PUMP 26 519118 14 u bui a 0 a ditus 27 OIL DISCHARGE MONITOR SLOPC 27 SMALL DIAMETER LINE pp 28 TANK CLEANING CRUDE OIL WASHING 28 SLOP DECANTING SYSTEM 29 TRANSFER SYSTEME Ne 29 MISCELLANEOUS TANKS 30 STEAM BOILER MAIN VARIABLEES
28. Q R 5 2 80 700372 lt 0 2 gt WTIP C D E P00326 bar L 0 1 0 1 WTIP F X00327 L 0 0 H 8 0 WTIP G X00330 WTIP H I M00331 kg WTIP J M00332 kg WTIP K L P00345 bar WTIP M P00346 bar WTIP N P00347 bar WTIP O P Z00368 DEG WTIP 700369 DEG WTIP R 5 42 IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 2 2 4 2 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT CHT2000 VLCC II ws Variable List 2 81 og U00412 L00411 U00410 V00402 V00401 M00403 M00405 G00450 SUAS OAS G00467 P00420 X00427 X00430 T00453 HaAROVOZ 2 82 00436 0437 00435 gt m g Q gt m Q lt E QN V00461 00462 00463 meZ Doc no SO 0606 A January 6 1997 0200 M CARGO TANK 2 MAIN VARIABLES m m3 h m3 h bar degC L 0 5 25 0 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 0 1 H 0 1 CT2 L 0 0 H 8 0 CT2 CT2 L 40 0 H 100 0 CT2 TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 30818 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSP
29. 30 23 C MERE 111 1 C MERE DECK LINE 1 Line venting 112 G 4 14 to deck line 2 G4761 6 P6 97 x 166 06 x 166 86 1 1 1 P1 99 P 0 58 P0 00 P 0 73 x 100 00 x 100 00 x 100 00 1 69 99 Crude oil Slop SHH COM S M suct suct X over X over X over X over line line line line 109 to bot line 2 CDC CHT2000 ULCC II REV 1 2 CHT2000 VLCC II ws User s Manual Page 5 54 5 5 5 5 1 5 5 2 5 5 3 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Discharging Procedure Operational Objectives Your Cargo Loss Control Program must aim at both maximising cargo outturn and closely monitoring cargo measurement Accordingly the objective of every discharge is to outturn the maximum quantity of cargo and to operate the highest safety and anti pollution standards Discharging sequence The discharge sequence should be performed in such a way that the vessel has good draining trim Le 5 6 meters in the initial stage of discharge Adequate draining trim will allow early effective stripping and leave minimal quantities in the tanks for final stripping Limiting Factors Draft Discharging Terminals usually have limited depth of water at the berth which may prevent the vessel from achieving a good draining trim until late in the discharging operation Page 5 55 CHT2000 VLCC II ws User s Manual Doc no S
30. 5 52 Checks after Loading 5 52 Laden V yates uu 5 52 Discharging PIOCEQUES s apa i 5 55 Operational ObjJectives a 5 55 Discharging sequere cadeuee 5 55 Limiting 5 55 1 5 57 Carso L ss 5 58 Instructions during and after Discharge 5 59 Iner ne Proced re Sonserina e cde ta EER 5 61 CE 5 61 nert Gas Polley ee 5 62 Inerting Empty i te HE eiit eai 3 03 Inerting during Deballastmig 5 64 Inerting during COW and Water Washing 5 64 Inerting during Loading 5 65 Inerting during Discharging 5 65 Inert Gas purging prior to Gas Freeing 5 65 G s Freeing tase AME 5 66 Inert Gas Emergency 5 67 5 69 Ballast Pump Ready ER 5 70 Seeregated Ballast 5 75 Dirty Ballast Departure Ballast a 5 76 Clean Ballast Arrival Ballast et 5 77 SIDpinocee 3 79 The SSCL PN 5 80 Bodas s RERO 5 81 The Vacuu
31. B Alarm Running 0 116 Slop Tanks Oil Discharge Monitor SLOP TANK SLOP TANK 6 P 139 CT 4 125 6 5 135 68 88 Balance line Ullage ua su 0 08 Cho E Sounding Yp R Ullage UB 59 Clean Oil Mix L2 67 Mix Water 18 00 Sounding L2u 71 66 69 Clean Oil Mix L2 32 TH Mix Water 12 99 68 00 ya eso __ 1188 Fron Eductor esed 99 L Equalizing line 80 08 Re X8 08 M 22 l 15 8 4 9 9 L lI ES High Overboard E X8 00 ppm Slop X over line P1 99 tot 60 00 Mavh oil 68 98 concent 80 00 flee 0 00 hksn n 199 from 68 09 169 00 1060 08 TG0 00 1 0 00 1060 08 S P COP 4 COP 3 COP 2 1 68 08 68 00 118 113 0 76 to Bottom line 3 CHT2000 ULCC II REV 1 2 The slop system consist of two slop tanks with WT 6P as primary slop tank and WT 65 secondary slop tank A decanting balance line is connected between the two slop tanks and an equalising line connects WT 6P to CT 4 All dirty ballast discharge from cargo tanks is monitored by the ODM Oil Discharge Monitor as regarded by IMO regulation Oil contaminated ballast with more than 15 PPM will be directed to port slop tank as long as the measured oil content is too high CHT2000 VLCC II ws User s Manual
32. COP1 GOVERNOR GAIN CONSTANT COP1 GOVERNOR RESET TIME CONSTANT Page 7 2 11 2135 RO2136 L02132 2130 002127 002125 002126 002171 G02172 G02170 Vn rub X02124 domNOWOZ 2 12 G02171 G02170 G02172 G02200 G02201 G02210 G02211 P02173 T02174 X02175 F Pt r 1 Q m P 2 Q Z gt P02203 T02204 X02205 30 72 OUO Page 8 Doc no SO 0604 A January 6 1997 Page 0013 M CARGO LINE 1 VACUUM SEPARATOR lt 0 1 gt lt 0 1 gt m bar m3 h m3 h m3 h m3 h m3 h m3 h L 1 0 H 5 0 COP1 VACUUM PUMP START COP1 VACUUM PUMP AUTO SWITCH COP1 SEPARATOR LEVEL COP1 SEPARATOR GAS PRESSURE abs COP1 SEPARATOR INLET LIQUID FLOW COP1 SEPARATOR GAS INFLUX COP1 VACUUM PUMP GAS FLOW FLOW FROM BOTTOM LINE 1 FLOW FROM CO SUCTION CROSSOVER FLOW FROM SW SUCTION CROSSOVER COP1 SEPARATOR OIL CONTENT Page 0014 M CARGO LINE 1 BOTTOM PIPING m3 h m3 h m3 h m3 h m3 h m3 h m3 h bar degC bar degC FLOW FROM BOTTOM LINE 1 FLOW FROM SW SUCTION CROSSOVER FLOW FROM CO SUCTION CROSSOVER TOTAL FLOW FROM 5 5 TOTAL FLOW FROM 5 TOTAL FLOW FROM CT 1 CROSS FLOW FROM BLIN2 PIPE LINE 1 PRESS aft PIPE LINE 1 TEMP aft PIPE LINE 1 OIL CONTENT aft PIPE LINE 1 PRESS fore PIPE LINE 1 TEMP fore PIPE LINE 1 OIL CONTENT fore CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2
33. L 05 25 0 TANK ULLAGE measured D U00212 m 1 05 H 25 0 WTIS TANK ULLAGE measured E U00312 m L 0 5 250 WTIP TANK ULLAGE measured F U00412 m L 0 5 250 2 TANK ULLAGE measured G U00512 m L 0 5 25 0 WT2S TANK ULLAGE measured H U00612 m L 0 5 250 WT2P TANK ULLAGE measured 1 U00712 L 0 5 25 0 WT3BS TANK ULLAGE measured J U01012 m L 0 5 250 WT3P TANK ULLAGE measured U01112 L 0 5 250 CT3 TANK ULLAGE measured L U01212 m L 0 5 250 WT4S TANK ULLAGE measured M U01312 m L 0 5 250 WT4P TANK ULLAGE measured N U01412 L 0 5 250 4 TANK ULLAGE measured 001512 L 0 5 25 0 WT5S TANK ULLAGE measured P U01612 m 1 0 5 250 WT5P TANK ULLAGE measured Q U01712 m L 0 5 250 WT6S TANK ULLAGE measured R U02012 m L 0 5 250 WT6P TANK ULLAGE measured 22 0101 01 TANK TOP OVERFLOW 2 2 600017 3 8 L 0 0 H 1 0 TANK OVERFLOW 600117 m3 s 1 00 H 1 0 TANK TOP OVERFLOW 600217 m3 s L 0 0 H 1 0 WTIS TANK TOP OVERFLOW 600317 m3 s 1 00 H 1 0 TANK TOP OVERFLOW G00417 m3 1 00 10 CT2 TANK TOP OVERFLOW G00517 m3 s L 0 0 10 WT2S TANK TOP OVERFLOW G00617 m3 s L 0 0 H 1 0 WT2P TANK TOP OVERFLOW 1 000717 m3s 1 00 H L0 WT3BS TANK TOP OVERFLOW J 001017 m3 s L 0 0 H 1 0 WT3BP TANK TOP OVERFLOW G01117 m3 s L 0 0 H 1 0 CT3 TANK TOP OVERFLOW L 601217 m3 s L 0 0 H 1 0
34. Page 58 Doc no SO 0604 A January 6 1997 Page 0312 M CARGO TANK WT 4 S FLOWS m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW PORT SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0313 M CARGO TANK WT 4 S LEVELS MASSES m m m m WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 14514 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List N 101253 V01256 001257 1260 1254 E01255 HP RPOMNOZEU ATT m Q m m 9 Q Z gt N um gt 201272 01226 01227 01230 01231 gt P01245 01246 P01247 Z01268 Z01269 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0314 M CARGO TANK WT 4 S HEATING degC m3 h kW kW kW L 40 0 H 100 0 WT4S CA
35. Page 69 N 601641 601642 G03265 001617 001643 001644 A G01633 G01634 lt G01670 2 136 001610 L01611 L01613 L01614 X01616 M01603 V01602 M01622 M01623 M01624 M01625 M01607 M01606 M01615 D01620 D01621 Q Z O 2 O Z lt i R r Q m i 9 Q Z gt Page 70 Doc no SO 0604 A January 6 1997 Page 0422 M CARGO TANK WT 5 P FLOWS m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WTS5P WTS5P BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION BW DROP FLOW INTO TANK WT5P WTSP WTSP WTSP WTSP WTSP WTSP TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0423 M CARGO TANK WT 5 P LEVELS MASSES m m m m WTS5P WTS5P WTSP WTSP WTSP WTSP WTS5P WTSP WTSP WTSP WTSP WTS5P WTSP WTS5P WTS5P WTS5P TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 8808 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List N U 101653 V01656 001657
36. at the tracker ball To rectify a suspected fault move the cursor to the variable in the Malfunction List ex M1301 and press the right hand push button of the Tracker ball The response from the computer will either be Repair Attempt or Malfunction Reset If the Malfunction log is turned on all attempts on repairing the fault are printed Page 5 16 5 2 3 2 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Variable List Displays a window with a list of all variables in the simulator All related information in organised in groups This means that all variables from the Cargo line system is located at pages starting at 0010 until 0017 The List can be scrolled moved or removed by using the select button of the tracker ball and cursor After pushing VARIABLE LIST identify sub system and press selected system Displayed window will then be identical to the variables found in the corresponding Model Drawing ex MD 02 at the monitor Tag details and measured values will be displayed Displayed data can be changed after clicking on values with centre tracker ball button After typing in new values and pressing enter new data is entered There are several ways to change the value of a model variable ex start stop of pumps One of them is using the Variable List Any pump or valve can be operated from this part of the simulator As the component to be operated is found move the cursor to the corresponding variab
37. it will be written ex M1301_S and you are allowed to continue In the section VALUE The active and passive values are entered When prompted type in values either digital 0 1 2 etc or analogue in percentage of max value Page 5 9 Doc no SO 0603 A 16 03 00 In the section ACTIVE The value entered is the new default as the fault is activated Selection of how the malfunction will be introduced continuos fault or repeating fault in the section AUTOMATIC MODE In the section PASSIVE The value entered is starting level at the time when the malfunction is activated UNIT Engineering unit or percentage Not necessary to be entered Under column AUTOMATIC MODE Activating this will make fault go active and stay active when entered time is reached Activating this button will make fault go active and then off again when time limits entered reached Activated this button will make fault go on and off repeatedly within specified time limits as long as scenario is run When activated time ramp for fault to develop can be specified CHT2000 VLCC II ws User s Manual Page 5 10 5 2 1 6 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Common for all four function buttons are that faults can be simulated after entering a scenario only when buttons are activated When active buttons change colour Ramp function can be active together with any of three other buttons Action
38. pop up From the variable page one can chose the following conditions for update Update Loadmaster from actual situation partly loaded Update Loadmaster with fully loaded ship Update Loadmaster with empty ship Update Simulator with Loadmaster condition Repeat functions for updating all tanks with equal parameters CHT2000 VLCC II ws User s Manual Page 5 24 Doc no SO 0603 A 16 03 00 5 3 3 5 3 3 1 5 3 3 2 5 3 3 3 CHT2000 VLCC II ws User s Manual General Operation How to change parameters and their influence on draft trim heel tank levels flow and the operation of pumps and valves are described in the following sections Draft The amidships draught is changed by changing the displacement The fore and aft drafts are changed by changing the displacement and or the trim Note This change will cause another load distribution resulting in another distribution of shear forces bending moments and hull deflection Trim The trim is changed by changing the load moments of the fore and aft halves of the ship Note This change will cause another load distribution which results in another distributing of shear forces bending moments and hull deflection Heel list The heel list is changed by changing the load moments in the wing tanks Page 5 25 Doc no SO 0603 A 16 03 00 00 00 00 Picture Rlarm Freeze m 131 Cargo Bargraph CONDITION DISPLACEMENT DEADWEIGHT DRAUGH
39. the Instructor Station during full simulation mode and from each workstation when in part task mode The pages in chapter 7 show the choice of malfunctions which can be introduced The two first pages comprises the Directory List while the rest of the pages contain the malfunctions available 4 3 Hull Models The content of liquid in the tanks will have an inevitable impact on the hull condition in terms of Hydrostatic conditions Draft Heel Trim Intact stability Meta centre height Hull Strain Shear force Bending moment Hull deflection These parameters are continuously computed based on currently updated tank levels and liquid densities In addition manually entered data will be computed and updated CHT2000 VLCC II ws User s Manual Page 4 27 Doc no SO 0603 A 9 January 1997 Basic hull design Based on outline specification on main geometrical data the following items have been computed Hydrostatics Loading conditions Light ship condition with Intact stability Shear force distribution Bending moment distribution Ballast condition with Intact stability Shear force distribution Bending moment distribution Full load condition with Intact stability Shear force distribution Bending moment distribution Longitudinal strength including limit values for Shear forces Bending moments Moment of inertia Bonjean tables CHT2000 VLCC II ws User s Manual Page 4 28 Doc no SO 0603
40. 0064 one can monitor and alter the discharge values However a total reset of the ODM can only be done if the ship state is in port condition ref page 0003 Sea ship state Page 5 91 Doc no SO 0603 A 16 03 00 01 39 58 Alarm Running HD 203 Inert Gas Plant Group DECK WATER SEAL 208 BOILER LINE NON pressure P0 09 A Boiler line HAZARDOUS HAZARDOUS HC X 1 63 temp T 360 00 AREA AREA flow 6 12017 81 83 MAIN LINE pressure P0 03 A open from deck HC 52 21 to Funnel piu 0 1 84 Vent Press RUTO 4_0 03 _ Ctr manje 926 Deck FAN 1 Water 1 START STOP Seal 66758 34 Main line meer 1 Overflow 10 35 A Drain 4 14 t FAN 2 Drain START STOP from Fire Pump open from deck CHT2000 ULCC II REV 1 5 UNIT PRINT CONVERSION REPORT CHT2000 VLCC II ws User s Manual Page 5 92 Doc no SO 0603 A 16 03 00 5 8 Inerting and Venting The operator can carry out and control the following operations Operation of inert gas plant and deck water seal Inerting of cargo tanks Ventilation gas freeing of cargo tanks The Inert Gas plant is operated from the picture MD 209 The Inert Gas plant is simplified compared to a real plant but most of the basic features are presented on the CHT2000 VLCC II ws The inertgas
41. 1 load line 1 valve V2226 leakage M1002 0 1 load 1 valve V2226 closed M1003 0 1 load line 2 valve V2426 leakage M1004 0 1 load line 2 valve V2426 closed M1005 0 1 load line 3 valve V2626 leakage M1006 0 1 load 3 valve V2626 closed M1007 0 1 load 4 valve V3026 leakage M1010 0 1 load line 4 valve V3026 closed r Q m m g Q gt Page 6 CHT2000 VLCC II ws Malfunction List M1101 M1102 M1103 M1104 M1105 M1106 M1107 M1110 demovozztm momsmguow ve MI201 M1202 M1203 M1204 M1205 M1206 M1207 M1210 r Q m m g Q gt demovozzgrcm Doc no SO 0605 A January 6 1997 Page 0900 MA09 BOTTOM LINE VALVES 0 1 bottom line 1 valve V2224 leakage 0 1 bottom line 1 valve V2224 closed 0 1 bottom line 2 valve V2424 leakage 0 1 bottom line 2 valve V2424 closed 0 1 bottom line 3 valve V2624 leakage 0 1 bottom line 3 valve V2624 closed 0 1 bottom line 4 valve V3024 leakage 0 1 bottom line 4 valve V3024 closed Page 1000 MA10 CARGO PUMP 1 2 0 100 0 100 Cargo pump 1 wear Cargo pump 1 LO filter dirty 0 100 Cargo pump 1 turbine wear 0 100 Cargo pump 1 governor unstable 0 100 Cargo pump 2 wear 0 100 Cargo pump 2 LO filter dirty 0 100 Cargo pump 2 turbine wear 0 100 Cargo pump 2 governor unstable ccc CHT2000 VLCC II ws Malfunction List Page 7 2 10 M1301 M1302 M1303 M1304 M1305 M1306 M1307
42. 13 Page 0015 M CARGO LINE 1 DECK PIPING A 602140 m3 h FLOW FROM TO DECK LINE 602156 m3 h FLOW FROM TO TC COW CROSSOVER D 602157 m3 h FLOW FROM COP1 TO SLOP CROSSOVER E 002141 m3 h LOAD FLOW to bottom line 1 602143 m3 h FLOW FROM SHORE TO MANIFOLD 1 H I 02146 bar DECK LINE 1 PRESSURE aft J T02147 degC DECK LINE 1 TEMPERATURE 2150 DECK LINE 1 OIL CONTENT aft L 2151 bar MANIFOLD 1 PRESSURE N T02152 degC MANIFOLD 1 TEMPERATURE O X02153 MANIFOLD 1 OIL CONTENT P 202154 kg m3 MANIFOLD OIL DENSITY Q R 5 2 14 Page 0016 M CARGO LINE 1 PUMP MONITOR PAGE A B C T03730 hour TOTAL PUMP RUNNING TIME D M03731 ktonn TOTAL PUMP FLOW MASS E E03732 MWh TOTAL COP ENERGY F G H M03733 tonn TOTAL TURBINE STEAM MASS I Z03734 US TOTAL STEAM COST J K L 5 CHT2000 VLCC II ws Variable List Page 9 2 15 C02260 C02261 C02262 C02263 C02264 C02265 AP POVOZEU ATE L Q T P 2 OQ Z gt 2 16 V12362 V12363 V02364 V02425 V02426 eo m g Q gt K V02422 L V02423 M V02420 V02421 V02424 V02427 Page 10 Doc no SO 0604 A January 6 1997 Page 0017 M CARGO LINE 1 PUMP DESIGN DATA COP1 PRESS CONSTANT 1 COP1 PRESS CONSTANT 2 COP1 PRESS CONSTANT 3 COP1 TORQUE CONSTANT 1 COP1 TORQUE CONSTANT 2 COP1 TORQU
43. 1900 AUTO 4 100 0 MAN 4 1900 MAN 4 100 0 MAN 4 1500 MAN Id 9 0 AUTO 4 1590 MAN 0 0 CHT2668 ULCC II REV 1 0 In the Cargo Pumping Diagram the actual pump and system curve are presented The curves are automatically updated when pump head pressure is increased Or decreased RPM is changed more pumps are started in the system and the NPSH value is changed due to increase in tank levels The pump RPM and discharge valve setting on each cargo pump can be operated from this mimic in order to optimise the pumping operation When a change is made new curves will appear leaving the previous curves dotted in order to analyse the variation CHT2000 VLCC II ws User s Manual Page 4 70 Doc no SO 0603 A 9 January 1997 4 8 Oil Gas Separator With Vacuum Pump The vacuum pumps can be run in auto or manual mode The cargo pumps are fitted with oil gas separators with vacuum pumps The vacuum pump is started automatically at low liquid level in the separator The state of the vacuum pump is shown by medium colour on the pump However if the liquid level in the oil gas separator gets too low vapour or air will enter into the pump and cause lost pumping capability and pump over speed This will be the case if the vacuum pump does not start automatically at low level Can be demonstrated by setting the vacuum pump in MANUAL Sp
44. 2 112 CHT2000 ULCC II REV 1 2 Cargo line 1 is from the manifold connected into CT and WT 5 P amp S pump room and cargo drop line and interconnected to 2 via branch line and isolating valve located in CT 1 From this mimic one will have a full overview of system no 1 during start up of cargo operations 4 5 12 Cargo Line 2 Cargo line 2 is from the manifold connected into CT 4 and WT 1 P amp S via the pump room and cargo drop line 2 and interconnected to line 3 via branch line and isolating valve located in CT 2 From this mimic one will have a full overview of system no 2 during start up of cargo operations CHT2000 VLCC II ws User s Manual Page 4 54 Doc no SO 0603 A 9 January 1997 4 5 13 Cargo Line 3 Cargo line 3 is from the manifold connected into CT 3 WT 2 P amp S and WT 6 P amp S via the pump room and cargo drop line 3 and interconnected to line 2 via branch line and isolating valve located in CT 2 From this mimic one will have a full overview of system no 3 during start up of cargo operations 4 5 14 Cargo Line 4 Cargo line 4 is from the manifold connected into CT 2 WT 4 P amp S pump room and cargo drop line 4 and interconnected to line 3 via branch line and isolating valve located in 2 From this mimic one will have a full overview of system no 4 during start u
45. 5 4 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Deballasting Unless otherwise specified the vessel should arrive load port with clean ballast and decanted slops in accordance with LOT procedures Load on Top procedures Unless Terminal local or international regulations require otherwise the vessel should deballast at sea prior to loading Simultaneous deballasting and loading of cargo tanks should not be attempted unless there is at least a two valve separation and the valves have been tested and found tight If the segregated ballast is sufficient to maintain the draft and freeboard limits required part cargo may be loaded prior to deballasting i e load deballast load During deballasting all possible clean ballast should be drained from the cargo tanks At the end of deballasting cargo lines should be drained into an after most cargo tank and stripped using the piston stripping pump If ballast is discharged to a shore reception facility then final discharge of ballast stripping must be performed using the Small Diameter Line Lining up Pipelines and Valves Prior to loading deck and pump room lines should be clearly arranged Cargo should flow through loading drop lines valves and bypass the pump room Pump room cargo line valves and sea suction valves should be firmly shut Deck valves which will not be used should be checked to ensure they are shut The position of all main valves stripping and
46. A 9 January 1997 Hydrostatics The current computation of hull hydrostatics at the actual load conditions is made by the hull simulation models The following parameters are computed Draught Trim Heel Draught The draught is adjusted until the weight of the displaced water equalise the light ship weight plus the cargo weight Wd WLS WC WLS WC dWg Aw V g dt CHT2000 VLCC II ws User s Manual Page 4 29 Doc no SO 0603 A 9 January 1997 Change in draught due to change in cargo When the weight of the cargo is changed the draught will be changed accordingly The change in draught can be estimated from the formula for displacement Tons Per Cm draught Wp pAw 0 01 Tons Cm This can be found in the tables and curve sheet for the hydrostatics w Trim Trim is adjusted until the trimming moment is equalised by the buoyancy moment from the displaced water The trimming moment is calculated for the Longitudinal Centre of Flotation LCF and the trimming is made at this point The location of the LCF is given by the shape and area of the hulls water plane at the actual draught as the total longitudinal moment of water plane area is to be equal to zero at the LCF L dAw 0 CHT2000 VLCC II ws User s Manual Page 4 30 Doc no SO 0603 A 9 January 1997 Change in the trim The amount of trimming can be estimated by means of the Moment To Trim 1 Cm MTC formu
47. Dirty water gradually over time Reducing Crude Oil Level in the Tank Discharging Clean oil Drip residue instantly Drip residue Clean oil gradually over time Increasing Crude Oil Level in the Tank Loading Drip residue Clean oil instantly CHT2000 VLCC II ws User s Manual Page 4 78 Doc no SO 0603 A 9 January 1997 Crude Oil Washing Washing oil Drip residue quick increasing Hard residue Clean oil gradually over time Soft residue Clean oil gradually over time Drip residue Clean oil slowly over time NB The COW efficiency is dependent on pressure of the washing media Tank Cleaning Water Washing Washing water Dirty water ref settling Hard residue Clean oil very slowly Soft residue Clean oil gradually over time NB The water washing efficiency is dependent on pressure and temperature of the washing water CHT2000 VLCC II ws User s Manual Page 4 79 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 CARGO HANDLING TRAINER CHT2000 VLCC II ws Chapter 5 Operation CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 OPERATION OF THE CHT2000 VLCC II ws Introduction This Chapter describes the operation of the Training and evaluation control TEC2000 basic cargo handling principles and operations general Cargo Operationi and documents standard procedures for loading discharging and inerting of the CHT2000 VLCC II w
48. EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE Scenario Displays different scenarios to be used during simulation classes Active in instructor mode only Instructor To create a scenario enter scenario by pressing SCENARIO button Prompts on screen will guide you onwards Push software button CREATE and click on a scenario button where you want it placed S01 to S20 After prompt and typing of scenario name press enter When entered name attaches to button scenario is accepted A prompt will then ask for an INITIAL condition to obtain parameters from Type in initial condition I01 to I60 and press enter If accepted prompt line will add initial conditions name and change colour When using instructors key pad left side group of buttons all the other available pages in editor are visible in top right corner of picture Clicking on any of these CHT2000 VLCC II ws User s Manual Page 4 9 Doc no SO 0603 A 9 January 1997 software buttons will bring you to this picture as would pressing any of same hardware buttons CHT2000 VLCC II ws User s Manual Page 4 10 Doc no SO 0603 A 9 January 1997 INSTRUCTOR n a OP OPERATOR INIT COND OPERATION SCENARIO DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING Init Conditions Directory FREEZE Displays recorde
49. H kon k nq k q H discharge head delivery press n relative pump speed q relative volume flow ko k and are design related constants The model variables H n and q are currently and dynamically up dated during the simulation while the model constants k and have to be set initially thereby designing the performance and the capacity of the pump The relationship between pump torque pump speed and pump flow can be described as T tin tq t4 T pump torque n relative pump speed q relative pump flow ti to t5 design related constants static friction constant For demonstration purposes the design related model constants of pump can be changed Ref Model Variable Directory page no 11 Cargo Pump 1 Design Data The power received from the Pump turbine can be expressed as PN while the power transferred to the liquid pumped can be expressed as Pour Hxq The pumps hydraulic efficiency can then be expressed as CHT2000 VLCC II ws User s Manual Page 4 69 Doc no SO 0603 A 9 January 1997 4 7 Cargo Pumping Diagram 01 56 07 Picture Alarm B Running 24 Cargo Pumping Diagram Group ohTE PUMP head 200 150 100 50 5000 10000 15000 20000 total flow 3 211 COPI setting 212 COP2 setting 213 COP3 setting 214 COP4 setting Speed Valve Speed Valve Speed Valve Speed Valve MAN 4
50. IG DECK SEAL SW LEVEL IG DECK SEAL SW PUMP NO 1 IG DECK SEAL SW DRAIN VALVE IG DISCHARGE LINE PRESSURE IG DISCHARGE LINE FLOW IG DISCHARGE LINE OXY CONTENT IG DISCHARGE LINE HC CONTENT IG ISOLATION IG OXYGEN AT ISOLATION IG PRESSURE AT ISOLATION CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 61 0090 M BALLAST TANK MAIN VARIABLES U00012 L 0 5 250 TANK ULLAGE measured FPT SOUNDING even keel FPT TANK ULLAGE even keel FPT TANK VOLUME cap 12113 m3 B B M00025 tonn FPT CLEAN WATER MASS lt 5 N eR V00035 FPT BOTTOM VALVE N 900040 BOTTOM OUTLET FLOW P G00017 m3 s L 0 0 1 0 FPT TANK TOP OVERFLOW Q R 5 2 62 Page 0091 M BALLAST TANK MISCELLANEOUS 00053 degC 1 40 0 H 100 0 TEMPERATURE D 00054 kW FPT HEAT LOSS TO SEA AIR F 00055 kW HEAT LOSS TO ADJACENT TANKS G H I 00045 LEVEL GAS PRESSURE J P00046 bar FPT GEODETIC PRESSURE P00047 bar FPT TOTAL TANK BOTTOM PRESSURE L 000021 kg m3 FPT WTR DENSITY at 15 dgrC N O P Q R S E CHT2000 VLCC II ws Variable List Page 33 2 63 og U00112 L00111 U00110 V00102 V00101 M00103 M00105 G00150 SUAS Oa G00167 P00126 X00127 X00130 00153 2 64 00136 00137 00135 Q m g OQ gt Tb dc 9
51. Interface program EMULA is driving the graphic pictures and installed individually on each workstation The OTISS program can run on any of the involved computers When it is running on the server the instructor can connect selected workstations for monitoring of the process by the students When more than one EMULA station is connected to one OTISS program the actions taken at one station will influence the shared process and the changes are observed on all the workstations This way of running the simulator is controlled by the instructor to avoid chaos if different operators take inconsistent actions The simulator is run in one of two modes as shown in figure 2 CHT2000 VLCC II ws User s Manual Page 1 5 Doc no SO 0603 A 9 January 1997 Man Machine Interface Mathematical Models Full Simulation Mode Man Machine Interface Mathematical Models Part Task Simulation Mode In the full simulation mode the OTISS program is run on the server and the instructor can select each workstation in the workstation room to be connected to the simulation In part task simulation mode the workstations are isolated from each other The OTISS program and the EMULA program will run on each workstation This mode is normally used for detailed studies of sub systems of the simulator Each workstation is also capable of running the complete simulation model i e several workstations can control the simulation without
52. L 40 0 L 40 0 L 40 0 L 40 0 L 40 0 L 40 0 L 40 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 H 100 0 CT1 CARGO TEMPERATURE WT1S CARGO TEMPERATURE WTIP CARGO TEMPERATURE CT2 CARGO TEMPERATURE WT2S CARGO TEMPERATURE WT2P CARGO TEMPERATURE CT3 CARGO TEMPERATURE WT4S CARGO TEMPERATURE WT4P CARGO TEMPERATURE CT4 CARGO TEMPERATURE WTSS CARGO TEMPERATURE WTSP CARGO TEMPERATURE WT6S CARGO TEMPERATURE WT6P CARGO TEMPERATURE Page 0505 M TANK SURVEY RESIDUES tonn tonn tonn tonn tonn tonn tonn tonn tonn tonn tonn tonn tonn tonn M04164 tonn TOTAL RESIDUES IN TANK WTIS TOTAL RESIDUES IN TANK WTIP TOTAL RESIDUES IN TANK CT2 TOTAL RESIDUES IN TANK WT2S TOTAL RESIDUES IN TANK WT2P TOTAL RESIDUES IN TANK CT3 TOTAL RESIDUES IN TANK WT4S TOTAL RESIDUES IN TANK WT4P TOTAL RESIDUES IN TANK CT4 TOTAL RESIDUES IN TANK WTS5S TOTAL RESIDUES IN TANK WTS5P TOTAL RESIDUES IN TANK WT6S TOTAL RESIDUES IN TANK WT6P TOTAL RESIDUES IN TANK TOTAL TANK RESIDUE CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 157 Page 0506 M TANK SURVEY ULLAGES A U00010 m FPT TANK ULLAGE even keel 000110 m TANK ULLAGE even keel U00210 WT1S TANK ULLAGE even keel D 000310 m WTIP TANK ULLAGE even keel E U00410 m CT2 TANK ULLAGE even keel F U00510 m WT2S TANK U
53. M CARGO TANK WT 6 S MISCELLANEOUS 0 2 bar L 0 1 L 0 0 H 0 1 H 8 0 M01731 kg M01732 kg bar bar bar DEG DEG WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 2 2 4 2 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT CHT2000 VLCC II ws Variable List N E A og U02012 L02011 U02010 V02002 V02001 M02003 M02005 G02050 lt t m Q a m G02067 P02026 X02027 X02030 T02053 N 2036 02037 2064 02061 L V02062 V02063 D EOM Doc no SO 0606 A January 6 1997 Page 0440 M CARGO TANK WT 6 P MAIN VARIABLES m m3 h m3 h bar degC 0 5 250 WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P 0 1 0 1 WT6P 1 0 0 H 8 0 WT6P WT6P L 40 0 H 100 0 WT6P TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 4024 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0441 M CARGO TANK WT 6 P
54. Master WT3BS TANK ULLAGE Load Master WT3BP TANK ULLAGE Load Master CT3 TANK ULLAGE Load Master WT4S TANK ULLAGE Load Master WT4P TANK ULLAGE Load Master CT4 TANK ULLAGE Load Master WTSS TANK ULLAGE Load Master WTSP TANK ULLAGE Load Master WT6S TANK ULLAGE Load Master WT6P TANK ULLAGE Load Master FHFO TANK ULLAGE Load Master AHFO TANK ULLAGE Load Master Page 0706 M LOAD MASTER MASSES FPT TANK MASS Load Master CTI TANKMASS Load Master WTIS TANK MASS Load Master WTIP TANK MASS Load Master TANK MASS Load Master WT2S TANK MASS Load Master WT2P TANK MASS Load Master WT3BS TANK MASS Load Master WT3BP TANK MASS Load Master CT3 TANK MASS Load Master WT4S TANK MASS Load Master WT4P TANK MASS Load Master CT4 TANK MASS Load Master WTS5S TANK MASS Load Master WTSP TANK MASS Load Master WT6S TANK MASS Load Master WT6P TANK MASS Load Master FHFO TANK MASS Load Master AHFO TANK MASS Load Master Page 89 Doc no SO 0604 A January 6 1997 2 175 Page 0707 M LOAD MASTER MISC TANKS A 06751 FHFO TANK VOLUME Load Master 06752 AHFO TANK VOLUME Load Master 06755 96 HFO SETTLING TANK VOLUME Load Master D 06756 HFO SERVICE TANK VOLUME Load Master 06757 DO STORAGE TANK VOLUME Load Master F 06758 96 DO SETTLING TANK VOLUME Load Master 06759 DO SERVICE TANK VOLUME Load Master
55. P E F G G03307 m3 h SMALL DIAM LINE FLOW H P03311 bar SMALL DIAM LINE PRESSURE deck I J X03312 96 SMALL DIAM LINE OIL CONTENT K L M N O P Q R 5 2 52 0070 M TANK CLEANING CRUDE OIL WASHING A B V03403 96 MAIN COW SUPPLY VALVE C P03400 MAIN COW LINE PRESSURE D 603402 m3 h MAIN COW LINE FLOW E F G H I J K L X03401 OIL CONCENTRATION IN TC COW FLOW Q R S T Page 28 CHT2000 VLCC II ws Variable List 2 S3 V03452 003450 03451 L03453 L03454 m a Q m a Q gt V03462 V03468 603460 03461 L03463 03464 ARANHVOZ 2 54 RO4103 04104 G04100 G04102 G04101 04002 V04110 M04111 L04112 L04113 Sh Oe SORE Q V04120 M04121 L04122 L04123 Doc no SO 0606 A January 6 1997 Page 0071 SLOP DECANTING SYSTEM BALANCE LINE VALVE m3 h BALANCE FLOW FROM PORT TO STBD SLOPT BALANCE LINE OIL CONTENT m BALANCE LINE OUTLET HEIGHT stbd m BALANCE LINE OUTLET HEIGHT port EQUALIZING LINE VALVE lt 0 1 gt EQUALIZING LINE SHUT OFF VALVE m3 h EQUALIZING FLOW FROM SLOPT P TO CT4 EQUALIZING LINE OIL CONTENT m EQUALIZING LINE OUTLET HEIGHT SLOP P m EQUALIZING LINE OUTLET HEIGHT CT4 Page 0073 M HFO TRANSFER SYSTEM lt 0 1 gt HFO TRANSFER PUMP START lt 0 1 gt TRANSFER SELECT 1 f
56. PRESS aft PIPE LINE 4 TEMP aft PIPE LINE 4 OIL CONTENT aft PIPE LINE 4 PRESS fore PIPE LINE 4 TEMP fore PIPE LINE 4 OIL CONTENT fore CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 37 Page 0045 M CARGO LINE 4 DECK PIPING A 602740 m3 h FLOW FROM COP4 TO DECK LINE 02756 m3 h FLOW FROM COP4 TO TC COW CROSSOVER D 002757 m3 h FLOW FROM COP4 TO SLOP CROSSOVER E F G02741 m3 h LOAD FLOW to bottom line 4 602743 m3 h FLOW FROM SHORE TO MANIFOLD 4 H I 2746 bar DECK LINE 4 PRESSURE aft J T02747 degC DECK LINE 4 TEMPERATURE K X02750 DECK LINE 4 OIL CONTENT aft L 2751 bar MANIFOLD 4 PRESSURE N T02752 degC MANIFOLD 4 TEMPERATURE X02753 90 MANIFOLD 4 OIL CONTENT 202754 kg m3 MANIFOLD OIL DENSITY Q R 5 2 38 Page 0046 M CARGO LINE 4 PUMP MONITOR PAGE A B T03760 hour TOTAL PUMP RUNNING TIME D M03761 ktonn TOTAL PUMP FLOW MASS E E03762 MWh TOTAL COP4 ENERGY F G H M03763 tonn TOTAL TURBINE STEAM MASS I Z03764 US TOTAL STEAM COST J K L 5 CHT2000 VLCC II ws Variable List Page 21 Doc no SO 0604 A January 6 1997 2 39 0047 M CARGO LINE 4 PUMP DESIGN DATA A B 03060 COP4 PRESS CONSTANT 1 D 03061 COP4 PRESS CONSTANT 2 03062 COP4 PRESS CONSTANT 3 F 03063 COP4 TORQUE CONSTANT 1 H 03064
57. Page 0413 M CARGO TANK WT 5 S LEVELS MASSES m m m m WTSS TANK ULLAGE even keel WTS5S SOUNDING even keel WTSS CLEAN OIL INTERFACE LEVEL WTSS CLEAN WTR INTERFACE LEVEL WT5S OIL CONTENT IN WTR OIL MIXTURE WTSS TOTAL TANK MASS incl residues WT5S TANK VOLUME cap 8808 m3 WTSS CLEAN OIL MASS WTSS DIRTY OIL MASS WTSS DIRTY WATER MASS WTSS CLEAN WATER MASS WT5S HARD RESIDUES WTSS SOFT RESIDUES WT5S DRIP RESIDUES WTS5S OIL DENSITY at 15 dgrC WT5S WTR DENSITY at 15 dgrC Page 67 N 9 01553 V01556 001557 E01560 E01554 E01555 HP RPONOZEU ATT m Q m m 9 Q Z gt N E N Z01572 P01526 X01527 X01530 M01531 ASS m Q m m 2 Q Z gt P01545 P01546 P01547 Z01568 Z01569 Page 68 Doc no SO 0604 A January 6 1997 Page 0414 M CARGO TANK WT 5 S HEATING degC m3 h kW kW kW L 40 0 H 100 0 55 CARGO TEMPERATURE WTSS CARGO HEATING STEAM VALVE WTSS WTSS WTSS WTSS CARGO HEATING STEAM FLOW HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS Page 0415 M CARGO TANK WT 5 S MISCELLANEOUS 0 2 bar L 0 1 L 0 0 H 0 1 H 8 0 kg M01532 kg bar bar bar DEG DEG WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 02 02 32 HYD
58. Page 0712 M Page 0713 M Page 0800 M Page 0900 M Page 0901 M Page 0902 M Doc no SO 0604 A January 6 1997 LOAD MASTER DENSITIES mputs 87 LOAD MASTER TEMPERATURES inputs 88 LOAD MASTER 5 0 88 LOAD NIASTER ULLAGES 89 LOAD MASTER MASSES Ne 89 LOAD MASTER MISC 90 LOAD MASTER DRAFT 90 LOAD MASTER HULL SHEAR FORCES 91 LOAD MASTER HULL BENDING MOMENTS 91 LOAD MASTER HULL DEFLECTIONS 92 LOAD MASTER HULL STABILITY 92 MOTION PLATFORM 93 SIM CONTROL INPUT ACCESS 93 SIM CONTROL TRIP STATE SURVEY 94 SIM CONTROL ALARM SYSTEM 94 CHT2000 VLCC II ws Variable List Page 0002 Page 0003 Page 0004 Page 0005 Page 0008 Page 0010 Page 0020 Page 0030 Page 0040 Page 0050 Page 0060 Page 0061 Page 0062 Page 0064 Page 0065 Page 0070 Page 0071 Page 0073 Page 0074 Page 0080 Page 0083 Page 0090 Page 0100 Page 0110 Page 0120 Page 0200 Page 0210 Page 0220 Page 0230 Page 0240 Page 0300 Page 0310 Page 0320 Page 0400 Page 0410 Page
59. Page 4 21 Doc no SO 0603 A 9 January 1997 Alarm Pages Pushing one of the buttons marked 1 to 28 will display a window on screen with system tag information List is divided into several columns CHT2000 VLCC II ws User s Manual Page 4 22 Doc no SO 0603 A 9 January 1997 MALFUNC VARIABLE ALARM LIST LIST LIST PICTURE MARK PREVIOUS DIRECTORY PICTURE PICTURE SELECT RECALL NEXT PICTURE MARKED P PICTURE ALARM ALARM ALARM ACKN LOG SILENCE Malfunction List Displays window with possible malfunctions directory page When main system is recognised a click on system button displays system list List can be scrolled or removed with cursor and centre trackerball button Active in both modes Operator Push button MALFUNCTION LIST and select subsystem by clicking on this Clicking on system will activate second window with system variables After location of suspected fault click on this lines COLON with RIGHT tracker ball button A prompt will identify tag and that a repair attempt is made CHT2000 VLCC II ws User s Manual Page 4 23 Doc no SO 0603 A 9 January 1997 Instructor As in operator mode but additional information displayed Clicking on selected lines COLON with LEFT trackerball button will toggle faults ON OFF When a fault is selected ON it will change colour and thus be identifiable Far right of each line is a numeric value in percentage Clicking on this with centre trackerba
60. Page 4 57 Doc no SO 0603 A 9 January 1997 4 5 17 Centre Tank 1 2 3 amp 4 Condition 01 32 48 Picture nye Alarm Running HD 122 Center Tank 1 Condition Group oris LIQUID Temp T59 19 Center Full Atnosphere lt 26 6 3 40 EX ULLRGE lt 222 60 00 A Measured v2 84 Am gas 100 00 3 gt res Eze 0802 74 P10 76 pom deck Crude Dil Washing SOUNDING meter Sea Water Washing Outlet Total L22 67 Valve eo P0 03 A Clean oil Mix Leo2 i OPEN 414 1990 Mix Hater 19 08 I CLOSE E Mixture x8 00 F 20 ole Perc of oil HASS tonnes Total M22083 i Clean Oil M22057 18 Dirty 011 M8 00 Dirty Water M0 00 heater Clean Mater M0 00 i 4 liquid level M soft hard Residues ton RESIDUES tonnes FS ea 2 8 8 8 9 9 Total M26 u8 5 55 55 M8 09 Sieh E 88 08 69 08 4 G2687 8 1 80 00 E8 00 Soft M9 95 208 n Drip M16 44 4 88 88 tot bobl flow 111 1119 182 Cargo Survey CHT2000 ULCC II REV 1 4 The centre tank picture gives a detailed description of the tank condition including the total mass of water oil or mixture in the tank Inert gas flow venting washing cow ing heating loading a
61. TANK WT5P T 2 44 Page 0054 M BALLAST WATER LINE PRESSURES A B C P04010 bar STATIC SW PRESSURE aft D E P03124 bar BW SEA CHEST PRESSURE F 03173 bar BW BOTTOM LINE PRESSURE aft G H P03122 bar BWP SUCTION PRESSURE I P03116 bar BWP DISCHARGE PRESS after choke J 146 BW DECK PRESSURE L 5 E Page 24 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 45 Page 0056 BALLAST WATER LINE PUMP MONITOR A B C T03770 hour TOTAL PUMP RUNNING TIME D M03771 TOTAL PUMP FLOW MASS E E03772 MWh TOTAL BWP ENERGY F G H M03773 tonn TOTAL TURBINE STEAM MASS I Z03774 US TOTAL STEAM COST J K L M N O P Q R 5 2 46 0057 M BALLAST WATER LINE PUMP DESIGN DATA A B C03250 BWP PRESS CONSTANT 1 D 03251 BWP PRESS CONSTANT 2 03252 BWP PRESS CONSTANT 3 F G 03253 BWP TORQUE CONSTANT 1 03254 BWP TORQUE CONSTANT 2 I 03255 BWP TORQUE CONSTANT 3 J K L 5 CHT2000 VLCC II ws Variable List Page 25 Doc no SO 0604 A January 6 1997 2 47 0060 M CROSS OVER LINES A P03350 bar CO SUCTION CROSSOVER PRESSURE P03351 bar SW SUCTION PORT CROSSOVER PRESSURE D 03352 bar TC COW CROSSOVER PRESSURE E P03353 bar SLOP CROSSOVER PRESSURE F P03358 bar SW SUCTI
62. To restart proceed according to the following steps Type the user s name in the LOGIN picture i e student1 and press ENTER After a while a new display appears and by means of the left push button select the VLCC II simulation plant A complete start up takes about 2 3 minutes When finished the instructor picture Init Condition appears Load the exercise wanted by pressing the middle button of the tracker ball at the Init Condition and proceed by pressing RUNNING Page 5 14 5 2 2 5 2 2 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Alarm Section Alarm Pages The central alarm system is compressed into the Alarm Section The alarm system has several push buttons with a corresponding red alarm indicator numbered from 1 through 28 Normally all alarm lamps are turned dark As soon as an alarm occurs one of the alarm lamps starts flashing Additional information is obtained by pressing the push button next to the flashing lamp Each lamp push button covers alarm points from dedicated sub systems The alarm point exceeded normal values turns into a flashing mode The Alarm point displayed in the MD picture turns to steady condition as soon as the operator moves the cursor to its location and resets the alarm by using the left hand side push button of the tracker ball As appropriate actions are carried out the alarm point previously indicated alarm condition turns off Measured values are display
63. VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT6P WT6P WT6P WT6P WT6P WT6P CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE STBD COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 75 N E gt G02041 G02042 G03371 G03370 G03472 G03450 G03460 G03345 G02017 Jn EE Pome a e 002043 002044 002033 002034 002070 2 148 U02010 L02011 L02013 L02014 X02016 M02003 V02002 M02022 M02023 M02024 M02025 M02007 M02006 M02015 D02020 D02021 Q Z O 2 O Z lt i R r Q m i 9 Q Z gt Page 76 Doc no SO 0604 A January 6 1997 Page 0442 M CARGO TANK WT 6 P FLOWS m3 h m3 h m3 h m3 h m3 h m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT6P BOTTOM OUTLET FLOW CNTR SUCTION WT6P BOTTOM OUTLET FLOW STBD SUCTION DIRTY BALLAST DISCHARGE TO SLOPT P FLOW FROM SLOPC TO ODM DIRTY oily DISCHARGE FLOW BALANCE FLOW FROM PORT TO STBD SLOPT EQUALIZING FLOW FROM SLOPT P TO CT4 EDUCTOR DISCHARGE FLOW WT6P TANK TOP OVERFLOW WT6P COW CLEANING FLOW WT6P SWW CLEANING FLOW WT6P INERT GAS FLOW FROM MAIN LINE WT6P INERT GAS FLOW TO DECK WT6P TOTAL SUCTION BOBBLE FLOW Page 0443 M CARGO TANK 6 LEVELS MASSES m m m m WT6P TANK ULLAGE even keel WT6P SOUNDING even keel WT6
64. WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 9283 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List 2 97 100653 V00656 G00657 E00660 E00654 E00655 AP Z Q 2 9 Z Z r ATT mn Q m m 9 Q gt 2 98 Z00672 P00626 X00627 X00630 M00631 m Q m m oO Q Z gt P00645 P00646 P00647 200668 Z00669 ARANHVOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0224 M CARGO TANK WT 2 P HEATING degC m3 h kW kW kW L 40 0 H 100 0 WT2P CARGO TEMPERATURE WT2P CARGO HEATING STEAM VALVE WT2P WT2P WT2P WT2P CARGO HEATING STEAM FLOW HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS 0225 CARGO TANK WT 2 P MISCELLANEOUS lt 0 2 gt bar L 0 1 L 0 0 H 0 1 H 8 0 kg M00632 kg bar bar bar DEG DEG WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 2 2 4 2 HYDRO
65. WT4S TANK TOP OVERFLOW 601317 m3 s L 0 0 10 WT4P TANK TOP OVERFLOW G01417 m3 s L 0 0 10 4 TANK TOP OVERFLOW G01517 m3 s L 0 0 10 WTSS TANK TOP OVERFLOW 601617 m3 s 1 00 H 1 0 WT5P TANK TOP OVERFLOW G01717 3 8 1 00 H 1 0 WT6S TANK TOP OVERFLOW G02017 m3 s L 0 0 H 1 0 WT6P TANK TOP OVERFLOW 5 CHT2000 VLCC II ws Alarm List Page 3 Page 4 Doc no SO 0604 A January 6 1997 CHT2000 VLCC II ws Alarm List Doc no SO 0604 A January 6 1997 2 3 Page 0200 AG02 TANK OXYGEN CONTENT 1 1 X00127 L 0 0 8 0 D X00227 L 0 0 8 0 15 OXYGEN CONTENT X00327 L 0 0 8 0 WTIP OXYGEN CONTENT F G X00427 L 0 0 H 8 0 CT2 OXYGEN CONTENT H X00527 L 0 0 H 8 0 WT2S OXYGEN CONTENT I X00627 L 0 0 H 8 0 WT2P OXYGEN CONTENT J X01127 L 0 0 H 8 0 CT3 OXYGEN CONTENT L X01227 L 0 0 H 8 0 WT4S OXYGEN CONTENT M X01327 L 0 0 H 8 0 WT4P OXYGEN CONTENT N O X01427 L 0 0 H 8 0 CT4 OXYGEN CONTENT P X01527 L 0 0 H 8 0 WTSS OXYGEN CONTENT X01627 L 0 0 H 8 0 WTSP OXYGEN CONTENT X01727 96 L 0 0 H 8 0 WT6S OXYGEN CONTENT S X02027 L 0 0 H 8 0 WT6P OXYGEN CONTENT T 2 4 Page 0400 AG04 TANK INERT GAS PRESSURE 1 1 P00126 bar L 0 1 0 1 TANK ATMOSPHERIC PRESSURE D P00226 bar 0 11 H 0 1 WTIS TANK ATMOSPHERIC PRESSURE E P00326 bar L 0 1 0 1 WTIP TANK ATMOSPHE
66. WT6S CARGO TEMPERATURE 02053 degC L 40 0 100 0 WT6P CARGO TEMPERATURE HANAHVOZ D a Page 0700 AG07 CARGO PUMP 1 SYSTEM 1 1 g Q Z gt X02247 0 5 L 0 0 1 0 COPI TRIP INDICATION E NO2110 rpm L 0 0 1950 0 SPEED F PO2115 bar L 0 0 200 DISCHARGE PRESS before choke G Z02107 1 00 H 40 0 COPI CAVITATION INDEX H I 2241 bar L 1 0 H 5 0 COP1 BEARING LO PRESSURE J T02242 degC 1 00 H 60 0 BEARING TEMPERATURE K L M L02132 m L 1 0 H 5 0 SEPARATOR LEVEL D EOM Page 6 CHT2000 VLCC II ws Alarm List a N02310 T02442 p gt gos X02647 E N02510 F P02515 G 702507 H I P02641 J T02642 K L L02532 danmovoz Doc no SO 0604 A January 6 1997 Page 0800 AG08 CARGO PUMP 2 SYSTEM 1 1 0 5 L 0 0 1 0 COP2 TRIP INDICATION rpm L 0 0 Hz1950 0 COP2 SPEED bar 1 00 200 COP2DISCHARGE PRESS before choke 1 00 400 2 CAVITATION INDEX bar 1 10 H 5 0 COP2 BEARING LO PRESSURE degC L 0 0 700 2 BEARING TEMPERATURE m 1 10 H 5 0 COP2 SEPARATOR LEVEL 0900 AG09 CARGO PUMP 3 SYSTEM 1 1 0 5 L 0 0 H 1 0 COP3 TRIP INDICATION rpm L 0 0 H 1950 0 COP3 SPEED bar L 0 0 200 DISCHARGE PRESS before choke 1 00 400 CAVITATION INDEX bar 1 10 H 5 0 COP3 BEARING LO PRESSURE degC L 0 0 H 70 0 BEARING TEMPERATURE m 1 10 H 5 0 COP3 SEPARATOR LEVEL CHT2000 VL
67. and ullages in the tank with cavitation of pumps if cargo transfer or COW operations is in progress It will also have effect on the stratification mixing of oil and water in the tanks Solar Time The Solar time is automatically following the Period in a 24 hour cycle and will begin at zero if not manually selected otherwise The solar time can be manually set in the Variable page 0003 Sea ship state The Solar time will have influence on the vapour CHT2000 VLCC II ws User s Manual Page 4 62 Doc no SO 0603 A 9 January 1997 pressure in the cargo tanks based on the temperature leakage from day night effect CHT2000 VLCC II ws User s Manual Page 4 63 Doc no SO 0603 A 9 January 1997 4 5 23 Boiler 81 38 05 Picture ne 298 Boiler Groep KIN 3 oe oF Presmra PB tar Efficiency 255 55 x 4 Feud Mater CHTXNW ULCE II REUS 19 UNIT CONVERS ON The oil fired boiler is equipped with two steam atomising oil burners that can produce approximately 50 ton hour steam at 15 bar and 410 C When the boiler is started it will automatically purge ignite and open for fuel regulate the water level etc Steam consumers are steam driven pumps and heaters in cargo tanks The flue gas from the boiler is also used for Inert Gas production The boiler can be iso
68. be carried out Press Freeze at TEC2000 panel Choose display INIT CONDITION and click on software button CREATE Type in name of the exercise to be saved in one of the vacant locations and press enter During the process of creating the exercise its name starts flashing After few seconds the new initial condition is made and the simulation can proceed by pressing Running To load an Init Condition press Freeze and click with centre tracker ball button on the Init Condition selected Loading is completed when the name of the exercise turns steady From this step the simulation can start on condition that Running is pressed Page 5 5 5 2 1 4 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Operating Condition This function allows the instructor to vary the external parameters the ship dynamics as well as internal processes In addition the instructor can introduce fixed values of selected variables By pressing this button an Instructor picture called Operating Condition is displayed This picture is divided into several groups where the following parameter can be altered Access Different access levels can be set Sound Control Allows the Instructor to control the volume of the Sound System in the Cargo control room where the operational simulator is installed if applicable Fixed process Instructor can introduce fixed process values for some of the major parameters in the systems Independent of consump
69. be followed Open the Starboard Slop Tank Bottom Valves Connect the starboard Slop Tank Bottom Valves to the Bottom line No 3 Slop tanks isolating valve Connect the suction side of cargo Pump No 3 or any other cargo pump to the Bottom Line Connect the discharge side of the actual cargo pump to Slop crossover line Start the cargo pump and open the discharge valve Put the Oil Discharge Monitor in operation Manual mode The Auto Overboard Valve and the Auto Recirculation Valve will remain open The Manual Overboard Valve to be kept open and the sloptank port dirty ballast inlet valve to be kept closed picture MD 116 If the Oil Discharge Monitor detects traces of oil an alarm will be given The Discharge Valve should be closed immediately recirculation Valve may be opened Page 5 90 5 7 16 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The Auto Overboard Valve will stay open and the Auto Recirculation Valve will stay closed as long as no oil is detected in the overboard Line Auto mode Both the Manual Overboard Valve and the Manual Recirculation Valve to remain open If oil is detected in the water the Auto Overboard Valve will close and the Auto Recirculation Valve will open An alarm will be given The valves will return to normal and the alarm will disappear as soon as no oil is detected in the water Oil Discharge Monitoring Variables From the ODM variable list page
70. bottom lines will be reduced By using the stripping valves while heeling and or trimming the ship a large amount of the remaining tank content can be stripped off Page 5 79 5 7 6 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The Stripping Pump The stripping pump can be started from control section of picture MD 216 by opening the steam supply valve When the pump is running the pump symbol will change colour There is no READY indication for this pump Speed Control The set point of the pump governor which regulates the pump speed is controlled by entering a new set point on the speed control section The stripping pump is basically used for stripping cargo from pumps and lines into the small diameter line on completion of discharging However the stripping pump can also be used to perform any kind of stripping from lines and or cargo tanks into cargo discharge lines and into both slop tanks through the Oil Discharge Monitor Stopping The pump is stopped by closing the steam supply valve with the right mouse button The turbine steam supply valve is closed and the pump is brought to stop after a while Page 5 80 5 7 7 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The Eductor The eductor is operated from the picture MD 216 provided one of the cargo pumps is running Open valves to enable the driving pump to suck water oil from the respective source and to deliver i
71. emptied by the stripping pump and discharged to the shore installation via the small diameter line NOTE If the air venting cock on the deck line is closed the draining of the deck line will not occur Procedure for stripping of deck line no n Keep the Cargo Pump no n stopped picture MD 211 214 Open the Deck Line Air Venting Cock picture MD 108 Keep open the Deck Line Valve picture MD 108 Open the TC COW X Over Valve picture MD 216 Open the TCOWC COSC connection Valve picture MD 216 Open the Stripping Pump Suction Valve picture MD 216 Page 5 83 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Open the Stripping Pump Discharge Valve picture MD 216 Open the Small Dia Line Manifold Valve picture MD 108 Start the Stripping Pump picture MD 216 Page 5 84 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 This page is intentionally left blank Page 5 85 Doc no SO 0603 A 16 03 00 Rag Slop Tanks Oil Discharge Monitor NOR SLOP TANK SLOP TANK NT P 139 CT 4 125 HT 6 5 135 60 00 Balance line Ullage Ua su d Sounding L24 77 Ullage 08 59 Clean 011 12 67 Mix Mater 0 00 Sounding 24 71 Clean 011 12 32 Mix Mater 21 60 08 P4 From Eductor 1 166 08 eer s Y 1 9 Equalizing line 68 08 8 68 1 6 6 8 4 0 0 High Overboard 0 00 ppm Slop X ov
72. plant must be started and tuned in due time before it is required to the tanks CHT2000 VLCC II ws User s Manual Page 5 93 Doc no SO 0603 A 16 03 00 5 8 1 Start up Procedures gt 11 13 14 15 Ensure that the oxygen analyser and Inert Gas pressure indicator are working Ensure the boiler is producing flue gas with an O2 content of 5 by volume or less Open IG control valve to Funnel 100 in manual mode Fill Scrubber and deckwater seal Check that the air suction valves to deck are closed Open fluegas supply valve to the scrubber Open IG fan suction valve Start IG fan Open IG fan discharge valve Observe the content before Deckseal to equalise with content in boiler Below 596 Open IG main control valve Open IG deck line supply valve Set the IG reciculation valve to AUTO mode or start closing the valve in MANUAL mode Click in the pressure control box to get a pop up diagram Observe content to deck seal equalise with content before Deckseal When content in deck line is OK open IG supply valves to the Cargo tanks CHT2000 VLCC II ws User s Manual Page 5 94 5 8 2 5 8 3 5 8 4 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Shut down procedure Open IG control valve to funnel 100 in MANUAL mode Shut of IG supply valves to cargo tanks Close Deckline supply valve and IG main control valve Shut down the blowers Cl
73. refilled with dry crude oil Following checks must be performed prior to COW operation Page 5 101 Doc no SO 0603 A 16 03 00 The Inert Gas plant is working properly and the oxygen content of delivered Inert Gas is below 5 by volume The oxygen content of tank s to be COW is below 8 90 by volume All cargo tanks have positive pressure The pressure in the COW line is as specified in the Manual The trim will be satisfactory when bottom washing is in progress as specified in the Manual Cargo pumps tanks and pipe lines are properly drained after completion of COW CHT2000 VLCC II ws User s Manual Page 5 102 5 9 1 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 COW Operation The COW is performed from the pictures MD 109 122 135 and 216 and is simulated in a simplified manner but so that the basic factors are accounted for In order to make the most out of the training the students should have basic knowledge of rules and regulations related to the COW operation Crude Oil Supply On off The crude oil supply is turned on and off by clicking the valves routing from the tank to the COW washing machine COW Start Stop The COW machine is started and stopped by clicking the COW supply valve on the tank condition mimic The tanks to be COW ed are selected from the workstation by means of clicking valve symbols Programming Tank cleaning machines The tank cleaning machines
74. specifically given FS Red The area under the stability curve from 0 to 40 degrees representing the Dynamic stability is shown in meter radians DS Rad CHT2000 VLCC II ws User s Manual Page 4 49 Doc no SO 0603 A 9 January 1997 4 5 7 Loading Discharging 00 16 25 Picture Alarm Running HD 17 Load Discharge oth LOADING LOAD DISCHARGE DISCHARGING Temp T60 00 deg C Density D820 00 kg m3 Connected Connected to manifold 4 3 2 1 to manifold 4 3 2 1 Pressure P5 89 bar Pressure P2 94 bar Drop Const P0 98 bar Rise Const P4 90 bar 198 68 98 G 2 90 D t 60 00 P7 74 68 98 P0 03 68 098 P 0 03 G 4771 P6 03 G u768 P6 63 P x 108 08 x 188 08 98 x 108 08 x 180 08 x 90 00 allt L 4 L 118 CHT2000 ULCC II REV 1 2 The picture gives information of shore terminal plant The proper selection loading discharging must be made prior to operation or by the instructor The manifold connections port or starboard must be selected by clicking on the connecting flanges with the left mouse button The pressure flow characteristics of the terminal is set by the instructor as well as cargo loading temperature and density CHT2000 VLCC II ws User s Manual Page 4 50 Doc no SO 0603 A 9 January 1997
75. specifications are not maintained condensation can accumulate causing damage to circuits when power is reapplied CHT2000 VLCC II ws User s Manual Page 3 2 Doc no SO 0603 A 9 January 1997 3 4 Main Power Requirements Provisions are made for routing cables Cable trays provides protection for the cables shielding from electromagnetic interference and retaining access to the cables for maintenance The modular nature of the simulator components dictates a large number of available power outlets If possible major components should be isolated from each other For example a fault in one room should not cause the loss of power in all rooms Similarly a failure in one room should not cause a power transient that would damage other parts of the computer system Power conditioning is also important especially if the local power sources do not provide the constant voltage and frequency required for system operation Voltage spikes may be undetected and do no visible harm when in fact the damage caused may be considerable and will only come to light as a serious failure later on Then the cause may be difficult or impossible to determine To avoid serious system failures an uninterrupted power supply UPS should be installed The Main supply to the electronic equipment should be taken from the buildings main supply The main supply cable should be protected from lightning by varistors All circuits should be protected by slow blow a
76. system clicking on system displays list of alarms in this system List can be scrolled moved or removed with cursor and centre trackerball button Instructor After pressing on ALARM LIST and identifying sub system window with list of alarms will be displayed Picture Directory Displays list of system pictures After recognition of system and clicking on this system picture will display on screen CHT2000 VLCC II ws User s Manual Page 4 25 Doc no SO 0603 A 9 January 1997 Mark Picture Clicking on this will mark picture for later recollection with RECALL MARKED PICTURE After clicking MARK PICTURE enter a chosen number After clicking RECALL MARKED PICTURE enter chosen number Select Picture Allows selection of picture after writing picture name in prompt Enter two letters and two digits without space Previous Picture Next Picture Allows scrolling to next previous picture in line as listed in picture directory Alarm Acknowledge Acknowledges external lights Alarm Log Displays active alarms To acknowledge all alarms displayed at once press EXTENDED CHAR button and A simultaneously Alarm Silence Shuts off alarm sound CHT2000 VLCC II ws User s Manual Page 4 26 Doc no SO 0603 A 9 January 1997 4 2 2 Fault System A comprehensive selection of malfunctions are available through the fault system Each sub system is provided with a large number of malfunctions These are selectable from
77. the deflection can then be expressed as follows The load distribution 1 40 14 4 The shear force 2 Q EIdy dx 2q0x C The bending moment 3 d y dx 2 q0x 2 C2 The inclination 4 ElIdy dx 2q0x 6 CI x 2 Cox CHT2000 VLCC II ws User s Manual Page 4 36 Doc no SO 0603 A 9 January 1997 The deflection 5 Ely q0x 244 6 2 2 C3 CA Where The integration constants will be dependent on the actual support of the beam and has to be decided in each particular case Example A beam with even load and free supports in both of the ends will have the following relationship between load distribution shear force bending moment including and deflection CHT2000 VLCC II ws User s Manual Page 4 37 Doc no SO 0603 A 9 January 1997 The Ship s Hull The ship s hull will differ from an even loaded beam in two ways The load distribution will not be even throughout the hull The cross section area and the corresponding moment of inertia will vary along the hull The load distribution along the hull will be q qls qc qb 91 Distributed weight light ship q Distributed weight cargo qb Distributed buoyancy A simple example on the relationship between the load distribution the shear force and bending moment is shown on the figure below M It is evident that a more detailed calculation of load distribution shear force b
78. the valve on the full tank permits precise control of the rate of loading of individual tanks The liquid level in topped off tanks should be checked frequently to make certain that the level is not rising because the tank valve is leaking or is not properly closed Page 5 51 5 4 11 5 4 12 5 4 13 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Final Tank The vessel should request the topping off rate before each tank reaches the pre determined ullage When ordering loading to stop time should be allowed for the terminal to shut down Space should be allowed in the tank for this and also for draining loading arms Checks after Loading As soon as loading is completed and the loading arms have been drained and disconnected the officer on duty student should ensure that all valves in the cargo system and appropriate tank openings are closed Laden Voyage During the laden voyage a positive Inert Gas pressure of at least 0 1 Bar should be maintained in the cargo tanks Topping up Inert Gas pressure during the voyage may be necessary When topping up the Inert Gas pressure in the cargo tanks particular attention should be paid to the O content The O content should be less than 5 by volume before the Inert Gas is introduced into the cargo tanks Page 5 52 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 This page is intentionally left blank Page 5 53 Doc no SO 0603 A 16 03 00
79. 0 H 70 0 H 1 0 COP4 BEARING LO PRESSURE COP4 BEARING TEMPERATURE COP4 RECIRCULATION VALVE POS COP4 LUB OIL PUMP START COP4 START STOP COP4 TRIP INDICATION COP4 SPEED SURGE CONTROL AUTO SWITCH COP4 FLOW SURGE CONTROL AUTO SWITCH COP4 GOVERNOR GAIN CONSTANT COP4 GOVERNOR RESET TIME CONSTANT Page 19 2 35 RO2735 RO2736 L02732 02730 002727 002725 002726 002771 G02772 G02770 in runi new a X02724 2 36 002771 002770 002772 903000 003001 003010 2773 L 2774 M X02775 P03003 T03004 X03005 ARANHVOZ Page 20 Doc no SO 0604 A January 6 1997 Page 0043 M CARGO LINE 4 VACUUM SEPARATOR lt 0 1 gt lt 0 1 gt m bar m3 h m3 h m3 h m3 h m3 h m3 h L 1 0 H 5 0 COP4 VACUUM PUMP START COP4 VACUUM PUMP AUTO SWITCH COP4 SEPARATOR LEVEL COP4 SEPARATOR GAS PRESSURE abs COP4 SEPARATOR INLET LIQUID FLOW COP4 SEPARATOR GAS INFLUX COP4 VACUUM PUMP GAS FLOW FLOW FROM BOTTOM LINE 4 FLOW FROM CO SUCTION CROSSOVER FLOW FROM SW SUCTION CROSSOVER COP4 SEPARATOR OIL CONTENT Page 0044 M CARGO LINE 4 BOTTOM PIPING m3 h m3 h m3 h m3 h m3 h m3 h bar degC bar degC FLOW FROM BOTTOM LINE 4 FLOW FROM SW SUCTION CROSSOVER FLOW FROM CO SUCTION CROSSOVER TOTAL FLOW FROM TANK WT 4 S TOTAL FLOW FROM TANK WT 4 P TOTAL FLOW FROM TANK CT 2 PIPE LINE 4
80. 0 M 2 160 Page 0512 M 2 161 Page 0520 M 2 162 Page 0521 M 2 163 Page 0600 M 2 164 Page 0601 M 2 165 Page 0602 M 2 166 Page 0603 M 2 167 Page 0604 M 2 168 Page 0700 M 2 169 Page 0701 M CHT2000 VLCC II ws Variable List CARGO TANK CT 4 MISCELLANEOUS 65 CARGO TANK WT 5 S MAIN VARIABLES 66 CARGO TANK WT 5 S 66 CARGO TANK WT 5 S FLOWS 67 CARGO TANK WT 5 S_ LEVELS MASSES 67 CARGO TANK WT 5 S HEATING 68 CARGO TANK WT 5 S MISCELLANEOUS 68 CARGO TANK WT 5 P MAIN VARIABLES 69 CARGO TANK WT 5 P 69 CARGO TANK WT 5 P FLOWS 70 CARGO TANK WT 5 P LEVELS MASSES 70 CARGO TANK WT 5 P 71 CARGO TANK WT 5 P MISCELLANEOUS 71 CARGO TANK WT 6 S MAIN VARIABLEES 72 CARGO TANK WT 6 S 72 CARGO TANK WT 6 S FLOWS 73 CARGO TANK WT 6 S 5 55 8 73 CARGO TANK WT 6 S HEATING 74 CARGO TANK WT 6 S MISCELLANEOUS 74 CARGO TANK WT 6 P MAIN VARIABLE
81. 00 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0122 M CARGO TANK WT 1 P FLOWS m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0123 M CARGO TANK 1 LEVELS MASSES m m m m WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 12554 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC Page 41 Doc no SO 0604 A January 6 1997 Page 0124 M CARGO TANK WT 1 P HEATING L 40 0 H 100 0 WTIP CARGO TEMPERATURE CARGO HEATING STEAM VALVE CARGO HEATING STEAM FLOW HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS 0125 CARGO TANK 1 MISCELLANEOUS 2 79 A B C D 00353 degC E V00356 WTIP F G00357 m3 h WTIP G H E00360 kW WTIP I E00354 kW WTIP J E00355 kW WTIP K L M N O P
82. 0111 703 Effictercy 26816 t Inder 20 00 X Shaft seesi 109090 1 F4 38 T 29 82 A ross p ore nei us EGET trip P P 6 CHT2NW ULCE II REUS 1 2 UNIT CONVERS ON The ballast pump is modelled as steam driven centrifugal pump The pump model is of a general type and can represent any steam driven centrifugal pump The pump drive unit is modelled to be steam driven turbine discharging the steam to a vacuum condenser CHT2000 VLCC II ws User s Manual Page 4 72 Doc no SO 0603 A 9 January 1997 4 8 2 Pump Room Cross over Lines Stripping Pump Eductor Tank Cleaning Heater 01 49 28 Picture Alarm Running 0 216 Stripping Pump Eductor Group 5 199 115 199 51 oon 228 15 31 cOW SHH ra 91602 0 B Educt uc or 63664 9 Slop tank 116 X 100 08 PORT t G 1461 9 68 88 pe Stripping Pump 60 00 1 80 00 P9 71 G8 00 pa d RI Dian 108 P1 39 P15 32 shaft speid 8 33 P1 65 ine 109 09 109 09 00 SPH creed 22020 109 09 100 00 Ctr 60 00 68 08 68 98 8 1468 pki inu gt line 4 5
83. 02505 HAAOVOZ 2 26 P02641 2642 g Q gt tri V02511 R02640 R02646 X02647 02533 R02534 02500 02666 ARAOVOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0031 M CARGO LINE 3 PUMP TURBINE m3 h bar bar bar L 0 0 rpm L 0 0 rpm kW 9 L 0 0 m3 h kWh kg H 20 0 COP3 DISCHARGE VALVE POS COP3 DISCHARGE VALVE POS COMMAND COP3 FLOW COP3 DISCHARGE PRESS before choke COP3 DISCHARGE PRESS after choke COP3 SUCTION PRESSURE H 1950 0 COP3 SPEED H 40 0 COP3 SPEED COMMAND COP3 POWER COP3 HYDRAULIC EFFICIENCY COP3 CAVITATION INDEX COP3 TURBINE STEAM CONTROL VALVE POS COP3 TURBINE SHAFT TORQUE TURBINE STEAM FLOW COP3 COP3 TURBINE EFFICIENCY Page 0032 M CARGO LINE 3 PUMP BEARING CONTROL bar L 1 0 degC L 0 0 lt 0 1 gt lt 0 1 gt lt 0 5 gt L 0 0 lt 0 1 gt lt 0 1 gt 5 0 H 70 0 H 1 0 COP3 BEARING LO PRESSURE COP3 BEARING TEMPERATURE COP3 RECIRCULATION VALVE POS COP3 LUB OIL PUMP START COP3 START STOP COP3 TRIP INDICATION COP3 SPEED SURGE CONTROL AUTO SWITCH COP3 FLOW SURGE CONTROL AUTO SWITCH COP3 GOVERNOR GAIN CONSTANT COP3 GOVERNOR RESET TIME CONSTANT Page 15 2 27 2535 RO2536 L02532 P02530 G02527 G02525 G02526 G02571 G02572 G02570 X02524 domHNOWOZ 2 28 G02571 G02570 G02572
84. 0420 Page 0430 Page 0440 Page 0500 Page 0510 Page 0512 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 H DIRECTORY LIST SIMULATOR TIME CONTROL SEA SHIP STATE SHORE CONNECTION DATA MANIFOLD PUMP WORK MONITOR CARGO LINE 1 CARGO LINE 2 CARGO LINE 3 CARGO LINE 4 BALLAST WATER LINE CROSS OVER LINES STRIPPING PUMP EDUCTOR OIL DISCHARGE MONITOR SLOPC SMALL DIAMETER LINE TANK CLEANING CRUDE OIL WASHING SLOP DECANTING SYSTEM HFO TRANSFER SYSTEM MISCELLANEOUS TANKS STEAM BOILER INERT GAS GENERATOR BALLAST TANK FP CARGO TANK CT 1 CARGO TANK WT 1 S CARGO TANK WT 1 P CARGO TANK CT 2 CARGO TANK WT 2 S CARGO TANK WT 2 P BALLAST TANK WT 3 S BALLAST TANK WT 3 P CARGO TANK CT 3 CARGO TANK WT 4 S CARGO TANK WT 4 P CARGO TANK CT 4 CARGO TANK WT 5 S CARGO TANK WT 5 P CARGO TANK WT 6 S CARGO TANK WT 6 P TANK SURVEY TANK COW VALVES P V BYPASS VALVES Page I H Page 0520 Page 0600 Page 0700 Page 0800 Page 0900 Page 2 Doc no SO 0604 A January 6 1997 PIPING OIL RESIDUES HULL LOAD MASTER MOTION PLATFORM CONTROL SIM CONTROL CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 VARIABLE LIST PAGES 2 1 Page 0002 M SIMULATOR TIME CONTROL A B X05014 0 1 GENERAL RESET COMMAND c time monitors C D E X05013 0 4 TIME FACTOR INDEX 0 4 input G 705000 SIMULATION TIME SCALE result I T05001 hour SIMULATION PERIOD J K
85. 0511 0 100 WTSS bottom valve V1535 leakage M0512 0 1 WTSS bottom valve V1535 closed M0513 0 1 WTSS bottom valve V1536 leakage 0514 0 1 WTSS bottom valve V1536 stuck M0515 0 100 WTSP bottom valve V1637 leakage M0516 0 1 WTSP bottom valve V1637 closed M0517 0 1 WTSP bottom valve V1636 leakage M0520 0 1 WTSP bottom valve V1636 stuck 3 e Z 2 9 Z Z T 8 m Q m F 9 Q Z gt p gt n Page 0600 MA06 WING TANK 6 VALVES M0601 0 100 WT6S bottom valve V1735 leakage M0602 0 11 WT6S bottom valve V1735 closed M0603 0 1 WT6S bottom valve V1736 leakage M0604 0 1 WTO6S bottom valve V1736 stuck M0605 0 100 WT6P bottom valve V2037 leakage M0606 0 11 WT6P bottom valve V2037 closed M0607 0 1 WT6P bottom valve V2036 leakage M0610 0 1 WT6P bottom valve V2036 stuck ri Q m m noB demovozzgrcnm CHT2000 VLCC II ws Malfunction List Page 5 Doc no SO 0604 A January 6 1997 a Page 0700 MA07 DECK LINE VALVES 0701 0 100 deck line 1 valve V2225 leakage 0702 0 1 deck 1 valve V2225 closed 0703 0 100 deck line 2 valve V2425 leakage 0704 0 1 deck 2 valve V2425 closed 0705 0 100 deck line 3 valve V2625 leakage 0706 0 1 deck line 3 valve V2625 closed 0707 0 100 deck line 4 valve V3025 leakage M0710 0 1 deck 4 valve V3025 closed lt lt lt lt lt lt lt lt lt AY Z Q tg Q Z Z l AST E Q m I Z AH p N a Page 0800 MA08 LOAD LINE VALVES M1001 0
86. 054 HULL DEFLECTION section 12 O P Q R S T 2 166 Page 0603 M HULL STABILITY A B L06060 m RIGHTING LEVER GZ 0 106061 RIGHTING LEVER GZ 5 dgr D L06062 m RIGHTING LEVER GZ 10 dgr E 106063 m RIGHTING LEVER GZ 15 dgr F L06064 m RIGHTING LEVER GZ 20 dgr G L06065 RIGHTING LEVER GZ 25 dgr H L06066 m RIGHTING LEVER GZ 30 dgr I L06067 m RIGHTING LEVER GZ 35 dgr J L06070 m RIGHTING LEVER GZ 40 dgr K L06071 m RIGHTING LEVER GZ 45 dgr L L06072 m RIGHTING LEVER GZ 50 dgr M L06073 m RIGHTING LEVER GZ 55 dgr N L06074 m RIGHTING LEVER GZ 60 dgr O P 106075 m METACENTRIC HEIGHT corrected Q L06076 m FREE SURFACE reduction R E06077 mrad DYNAMIC STABILITY area 0 40 dgr S T CHT2000 VLCC II ws Variable List Page 85 2 167 L04011 L04012 L04015 L04016 L04013 L04014 Z04166 Sen Y mu 04151 2 168 X06799 X06798 D74001 T74000 U06784 X06785 X06786 06787 X06788 X06789 SO ATE m Q m m 9 Q Z gt D06790 X06791 X06792 T06793 X06794 X06795 Page 86 Doc no SO 0604 A January 6 1997 0604 HULL DRAFT BEES B B M04165 ktonn M04167 ktonn M04163 ktonn M04150 tonn tonn M04152 tonn DRAFT AFT DRAFT FORE DRAFT STBD DRAFT PORT HULL TRIM HULL HEEL DEADWEIGHT relative DEADWEIGHT DIS
87. 1 2 99 Page 0230 M BALLAST TANK WT 3 S MAIN 32 2 100 0231 M BALLAST TANK WT 3 S MISCELLANEOUS 52 2 101 Page 0240 M BALLAST TANK WT 3 P MAIN 53 2 102 Page 0241 BALLAST TANK WT 3 P MISCELLANEOUS 53 2 103 Page 0300 M CARGO TANK CT 3 MAIN VARIABLES 54 2 104 0301 CARGO TANK 3 VALWVES 54 2 105 Page 0302 M CARGO TANK CT 3 55 2 106 Page 0303 M CARGO TANK CT 3 LEVELS MASSES 23 2 107 Page 0304 M CARGO TANK CT 3 HEATING 56 2 108 Page 0305 M CARGO TANK CT 3 MISCELLANEOUS 56 2 109 Page 0310 M CARGO TANK WT 4 S MAIN VARIABLES 37 2 110 0311 M CARGO TANK WT 4 S VALWVES 37 2 111 Page 0312 M CARGO TANK WT 4 S FLOWS 58 2 112 Page 0313 M CARGO TANK WT 4 S LEVELS MASSES 58 2 113 Page 0314 M CARGO TANK WT 4 S HEATING 59 2 114 Page 0315 M CARGO TANK WT 4 S MISCELLANEOUS 39 2 115 Page 0320 M CARGO TANK WT 4 P MAIN VARIABLES 60 2 116 Page 0321 M CARGO TANK WT 4 P 60 2 117 Page 032
88. 122 2169 rpm 0 40 bar 80 Deg C 250 mWC 0 4 mWC 122 2169 rpm 0 40 bar 80 Deg C 250 mWC Page 1 2 Doc no SO 0603 A 6 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Appendix B Alarm List Doc no SO 0604 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 6 January 1997 2 APPENDIX ALARM LIST CHT2000 VLCC II ws User s Manual Doc no SO 0604 A January 6 1997 TABLE OF CONTENTS Section Page 1 DIRECTORY LIST Ems 1 1 1 Page 0100 TANK ULLAGE 2 1 1 2 Page 0400 TANK INERT GAS PRESSURE 1 page 1 2 VARIABLE LIST PAGES 3 2 1 Page 0100 AG01 TANK ULLAGE 1 2 3 2 2 Page 0101 AGO1 TANK TOP OVERFLOW 2 2 3 2 3 Page 0200 AGO2 TANK OXYGEN CONTENT 1 1 5 2 4 Page 0400 AG04 TANK INERT GAS PRESSURE 1 1 5 2 3 Page 0500 05 TANK CARGO TEMPERATURE 1 1 6 2 6 Page 0700 AGO7 CARGO PUMP 1 SYSTEM 1 1 6 2 7 Page 0800 08 CARGO PUMP 2 SYSTEM 1 1 7 2 8 Page 0900 AG09 CARGO PUMP 3 SYSTEM 1 1 7 2 9 Page 1000 AG10 CARGO PUMP 4 SYSTEM 1 1 8 2 10 Page 1100 AG11 BALLAST PUMP SYSTEM 1 1 8 2 11 Page 1300 AG13 HULL BENDING MOMENTS 1 1
89. 1457 m3 h CT4 CARGO HEATING STEAM FLOW H I 01460 kW CT4 HEAT FROM STEAM J 1454 kW CT4 HEAT LOSS TO SEA AIR E01455 kW CT4 HEAT LOSS TO ADJACENT TANKS L M N O P Q R S T 2 126 Page 0405 M CARGO TANK 4 MISCELLANEOUS 701472 lt 0 2 gt IG INITIATION 2 IG C D 1426 L 0 1 H 0 1 CT4 TANK ATMOSPHERIC PRESSURE F X01427 L 0 0 8 0 CT4 OXYGEN CONTENT G X01430 CT4 HYDRO CARBON CONTENT H 01431 INERT GAS MASS 02 CO2 N2 J 01432 kg CT4 HYDRO CARBON MASS K L P01445 bar CT4 LIQUID GAS PRESSURE M P01446 bar CT4 GEODETIC PRESSURE N P01447 bar CT4 TOTAL TANK BOTTOM PRESSURE O P Z01468 DEG CT4 TANK CLEANING UPPER LIMIT Q Z01469 DEG CT4 TANK CLEANING LOWER LIMIT R S T CHT2000 VLCC II ws Variable List Page 65 N N og U01512 L01511 U01510 V01502 V01501 01503 01505 001550 SUAS G01567 P01526 X01527 X01530 T01553 domHOovVoz N N o V01536 V01535 V01564 V01568 V01561 V01562 V01563 Z O 2 O Z lt i R r Q m i 9 Q Z gt Page 66 Doc no SO 0604 A January 6 1997 0410 M CARGO TANK WT 5 S MAIN VARIABLES m m3 h m3 h bar degC L 0 5 250 WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS WTSS 0 1 0 1 WTSS L 0 0 8 0 WTSS WT5S L 40 0 100 0 WTSS TANK ULLAGE measured
90. 2 lt 0 1 gt CT4 INERT GAS OUTLET VALVE P V bypass M V01262 lt 0 1 gt WT4S INERT GAS OUTLET VALVE P V bypass 01362 lt 0 1 gt WT4P INERT GAS OUTLET VALVE P V bypass O P 01562 lt 0 1 gt WTSS INERT GAS OUTLET VALVE P V bypass Q V01662 0 1 WTSP INERT GAS OUTLET VALVE P V bypass 1762 0 1 WT6S INERT GAS OUTLET VALVE P V bypass S V02062 0 1 WT6P INERT GAS OUTLET VALVE P V bypass T Page 82 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 161 Page 0520 M PIPING OIL RESIDUES 1 A B X02175 PIPE LINE 1 OIL CONTENT C X02205 PIPE LINE 1 OIL CONTENT fore D 2150 96 DECK LINE 1 OIL CONTENT X02153 96 MANIFOLD 1 OIL CONTENT F X02375 PIPE LINE 2 OIL CONTENT H X02405 PIPE LINE 2 OIL CONTENT fore I X02350 DECK LINE 2 OIL CONTENT aft J X02353 MANIFOLD 2 OIL CONTENT K L X02575 PIPE LINE 3 OIL CONTENT aft M X02605 PIPE LINE 3 OIL CONTENT fore X02550 96 DECK LINE 3 OIL CONTENT X02553 MANIFOLD 3 OIL CONTENT P X02775 PIPE LINE 4 OIL CONTENT aft R X03005 PIPE LINE 4 OIL CONTENT fore S X02750 DECK LINE 4 OIL CONTENT aft T X02753 MANIFOLD 4 OIL CONTENT 2 162 Page 0521 M PIPING OIL RESIDUES 2 X02124 SEPARATOR OIL CONTENT D 02324 COP2 SEPARATOR OIL CONTENT E X02524 COP3 SEPARATOR OIL CONTENT F X02724 COP4 SE
91. 2 M CARGO TANK WT 4 P FLOWS 61 2 118 Page 0323 M CARGO TANK WT 4 P LEVELS MASSES 61 2 119 Page 0324 M CARGO TANK WT 4 P 62 2 120 Page 0325 M CARGO TANK WT 4 P MISCELLANEOUS 62 2 121 Page 0400 M CARGO TANK CT 4 MAIN VARIABLES 63 2 122 0401 M CARGO TANK CT 4 VALVES 63 2 123 Page 0402 M CARGO TANK CT 4 64 2 124 Page 0403 M CARGO TANK CT 4 LEVELS MASSES 64 2 125 Page 0404 M CARGO TANK CT 4 HEATING 65 Page iv CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 126 Page 0405 M 2 127 Page 0410 M 2 128 Page 0411 M 2 129 Page 0412 M 2 130 Page 0413 M 2 131 Page 0414 M 2 132 0415 2 133 Page 0420 M 2 134 Page 0421 M 2 135 Page 0422 M 2 136 Page 0423 M 2 137 Page 0424 M 2 138 Page 0425 M 2 139 Page 0430 M 2 140 0431 2 141 Page 0432 M 2 142 Page 0433 M 2 143 Page 0434 M 2 144 Page 0435 M 2 145 Page 0440 M 2 146 Page 0441 M 2 147 Page 0442 M 2 148 Page 0443 M 2 149 Page 0444 M 2 150 Page 0445 M 2 151 Page 0500 M 2 152 Page 0501 M 2 153 Page 0502 M 2 154 Page 0503 M 2 155 Page 0504 M 2 156 Page 0505 M 2 157 Page 0506 M 2 158 Page 0507 M 2 159 Page 051
92. 2461 02462 02463 02464 02465 3 2 Q 2 9 Z Z F 8 r L Q T P Z OQ Z gt 2 24 12562 V12563 V02566 V02564 V02625 V02626 V02622 V02623 V02620 02621 F Ea Gy m In gt V02624 V02627 V02628 V02630 V02631 V02638 14 Doc no SO 0604 A January 6 1997 Page 0027 M CARGO LINE 2 PUMP DESIGN DATA COP2 PRESS CONSTANT 1 COP2 PRESS CONSTANT 2 COP2 PRESS CONSTANT 3 5 COP2 TORQUE CONSTANT 1 COP2 TORQUE CONSTANT 2 COP2 TORQUE CONSTANT 3 Page 0030 M CARGO LINE 3 VALVES lt 0 1 gt MANIFOLD 3 SHUT OFF VALVE stbd lt 0 1 gt MANIFOLD 3 SHUT OFF VALVE port lt 0 1 gt MANIF 3 4 CROSSOVER VALVE lt 0 1 gt MANIFOLD 3 DRAIN VALVE DECK LINE 3 SHUT OFF VALVE lt 0 1 gt LOAD LINE 3 SHUT OFF VALVE lt 0 1 gt TC COW CROSSOVER VALVE lt 0 1 gt SLOP CROSSOVER VALVE lt 0 1 gt CO SUCTION CROSSOVER VALVE lt 0 1 gt SW SUCTION CROSSOVER VALVE lt 0 1 gt BOTTOM LINE 3 SHUT OFF VALVE lt 0 1 gt BOTTOM LINE 3 4 CONNECTION VALVE lt 0 1 gt BOTTOM LINE 3 4 CONNECTION VALVE lt 0 1 gt FORE BOTTOM LINE 3 ISOLATION VALVE lt 0 1 gt LOAD LINE 3 CT 3 ISOLATION VALVE lt 0 1 gt LOAD LINE 3 CT 3 ISOLATION VALVE CHT2000 VLCC II ws Variable List 2 25 V02512 V02513 G02514 P02515 P02516 2522 02510 2501 E02520 702521 202507 SUAS 02503 002506 002504 2
93. 3 Line 3 Inert Gas Plant Wing Tank 5 Stb Atmosphere Line 4 1 Inert Gas Distribution 235 Wing Tank 6 Stb Atmosphere Ballast Line 21 Ballast Line 211 Crude Oil Pump Discharge Monitor Diagram 1 Condition ewer 2 Condition 3 Condition Legend 4 Condition Pump Eductor Cow Sw TP Port Condition EN Port Condition LOAD MASTER 3 4 5 6 7 8 9 10 11 12 1 8 9 0 2 3 4 1 6 9 0 1 114 115 116 CHT2000 VLCC II ws User s Manual Page 4 41 Doc no SO 0603 A 9 January 1997 The Directory will give the operator overview of all process pictures From this directory any picture can be selected including the Load Master directory On the following pages you will find simplified drawings of the process pictures according to the directory CHT2000 VLCC II ws User s Manual Page 4 42 Doc no SO 0603 A 9 January 1997 4 5 1 Cargo Bargraph 00 00 00 Picture Alarm BN NOR Freeze HD 191 Cargo Bargraph Group ON CONDITION DISPLACEMENT DEADWEIGHT DRAUGHT meter STABILITY meter Sea Density 0 1925 0 1888 ton 210 35 1888 ton 180 73 Aft 1 18 51 GM Corr L5 50 Sea temp 25 00 X of V 96 17 Mid STBO L 18 30 FS Red 10 72 summer mark Mid PORT L 18 30 OS Rad E 14 91 Fwd L 18 09 Trim 10 43 Heel 1 0 00 PORT CENTER STARBOARD 100 WT6P WTSP WT4P WT3P WT2P WTIP CT4 CT3 CT2 CT1 FPT W
94. 3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 CT1 CT1 CT1 CT1 CT1 CT1 CT1 CT1 CT1 BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION BOTTOM OUTLET FLOW PORT SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0103 M CARGO TANK CT 1 LEVELS MASSES m m m m CTI CTI TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 30813 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC Page 35 Doc no SO 0604 A January 6 1997 2 67 0104 M CARGO TANK 1 HEATING A B C 00153 degC 1 40 0 H 100 0 CARGO TEMPERATURE E 00156 96 CT1 CARGO HEATING STEAM VALVE G00157 m3 h CARGO HEATING STEAM FLOW H I 00160 kW HEAT FROM STEAM J 00154 kW HEAT LOSS TO SEA AIR K E00155 kW HEAT LOSS TO ADJACENT TANKS L M N O P Q R S T 2 68 Page 0105 M CARGO TANK CT 1 MISCELLANEOUS A 700172 lt 0 2 gt IG INITIATIO
95. 35 leakage D M0304 0 1 WT3BS bottom valve V0735 closed E M0305 0 100 WT3P bottom valve V1035 leakage F M0306 0 1 bottom valve V1035 closed lt lt AT EO 9 Page 0400 04 WING TANK 1 2 VALVES M0401 0 100 WTIS bottom valve V0235 leakage M0402 0 11 WTIS bottom valve 0235 closed M0403 0 1 WTIS bottom valve V0236 leakage M0404 0 1 WTIS bottom valve V0236 stuck M0405 0 100 WTIP bottom valve V0337 leakage M0406 0 1 WTIP bottom valve V0337 closed M0407 0 1 WTIP bottom valve V0336 leakage M0410 0 1 WTIP bottom valve V0336 stuck M0411 0 100 WT2S bottom valve V0535 leakage M0412 0 1 WT2S bottom valve V0535 closed M0413 0 1 WT2S bottom valve V0536 leakage M0414 0 1 WT2S bottom valve V0536 stuck M0415 0 100 WT2P bottom valve V0637 leakage M0416 0 1 WT2P bottom valve V0637 closed M0417 0 1 WT2P bottom valve V0636 leakage M0420 0 11 WT2P bottom valve V0636 stuck demovozgum mommuosg Page 4 CHT2000 VLCC II ws Malfunction List Doc no SO 0605 A January 6 1997 2 4 Page 0500 MA05 WING TANK 4 5 VALVES M0501 0 100 45 bottom valve V1235 leakage M0502 0 1 WTAS bottom valve V1235 closed M0503 0 1 WTAS bottom valve V1236 leakage 0504 0 1 WTAS bottom valve 1236 stuck M0505 0 100 bottom valve V1337 leakage M0506 0 1 WT4P bottom valve V1337 closed M0507 0 1 WTAP bottom valve V1336 leakage M0510 0 1 WT4P bottom valve V1336 stuck M
96. 3533 V03538 V03532 03554 03555 X03556 X03557 L03534 R03536 V03535 P03550 G03551 X03552 X03553 Z r r Q m m Q gt V03563 X03564 P03565 ARAN VOZ Page 32 Doc no SO 0604 A January 6 1997 Page 0083 M INERT GAS GENERATOR 1 lt 0 1 gt lt 0 1 gt lt 0 1 gt m3 h degC lt 0 1 gt lt 0 1 gt degC lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt 1 0 2 L 20 0 100 0 1 5 IG SCRUBBER PUMP SEA CHEST VALVE IG SCRUBBER PUMP DISCHARGE VALVE IG SUPPLY LINE SHUT OFF VALVE IG SUPPLY LINE GAS FLOW IG SUPPLY LINE GAS TEMP IG SUPPLY LINE OXY CONTENT IG SCRUBBER PUMP IG SCRUBBER SW DRAIN VALVE IG SCRUBBER SW LEVEL IG SCRUBBER GAS OUTLET TEMP IG FAN 1 START IG FAN 1 DISCHARGE VALVE IG FAN 1 AIR SUCTION VALVE IG FAN 1 GAS SUCTION VALVE IG FAN 2 START IG FAN 2 DISCHARGE VALVE IG FAN 2 AIR SUCTION VALVE IG FAN 2 GAS SUCTION VALVE Page 0084 M INERT GAS GENERATOR 2 lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt m lt 0 1 gt lt 0 1 gt bar m3 h lt 0 1 gt bar L 0 0 L 0 0 H 0 1 H 7 0 H 0 8 H 0 1 H 6 0 DECK SEAL PUMP SEA CHEST VALVE DECK SEAL PUMP DISCHARGE VALVE IG CONTROL VALVE IG MAIN CONTROL VALVE IG VENT VALVE IG DECK LINE SUPPLY VALVE IG DECK LINE GAS PRESSURE IG DECK LINE OXY CONTENT IG DECK LINE HC CONTENT
97. 450 L06451 L06452 L06453 L06454 SUAS n Q m m Q 2 gt N o 106460 L06461 L06462 L06463 L06464 L06465 L06466 L06467 L06470 L06471 L06472 L06473 N L06474 lt SORE Q Z gt O P L06475 Q L06476 R E06477 S 5 Page 92 Doc no SO 0604 A January 6 1997 Page 0712 M LOAD MASTER HULL DEFLECTIONS BBBBBBBBBBBBB HULL DEFLECTION section 0 LM HULL DEFLECTION section 1 LM HULL DEFLECTION section 2 LM HULL DEFLECTION section 3 LM HULL DEFLECTION section 4 LM HULL DEFLECTION section 5 LM HULL DEFLECTION section 6 LM HULL DEFLECTION section 7 LM HULL DEFLECTION section 8 LM HULL DEFLECTION section 9 LM HULL DEFLECTION section 10 LM HULL DEFLECTION section 11 LM HULL DEFLECTION section 12 LM 0713 M LOAD MASTER HULL STABILITY HBHBHBHBHBBBSHHBHBHBBBSB mrad RIGHTING LEVER GZ 0 dgr LM RIGHTING LEVER GZ 5 dgr LM RIGHTING LEVER GZ 10 dgr LM RIGHTING LEVER GZ 15 dgr LM RIGHTING LEVER GZ 20 dgr LM RIGHTING LEVER GZ 25 dgr LM RIGHTING LEVER GZ 30 dgr LM RIGHTING LEVER GZ 35 dgr LM RIGHTING LEVER GZ 40 dgr LM RIGHTING LEVER GZ 45 dgr LM RIGHTING LEVER GZ 50 dgr LM RIGHTING LEVER GZ 55 dgr LM RIGHTING LEVER GZ 60 dgr LM METACENTRIC HEIGHT correct
98. 510 V00502 V00501 M00503 M00505 G00550 SUAS OAS G00567 P00526 X00527 X00530 T00553 domHOovoz 2 88 V00536 V00535 Q m m g Q gt H V00564 I V00568 J 00561 L V00562 V00563 AP ANH MVOZ Page 46 Doc no SO 0604 A January 6 1997 0210 M CARGO TANK WT 2 S MAIN VARIABLES m m3 h m3 h bar degC 105 25 0 WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S 0 1 0 1 WT2S 1 0 0 H 8 0 WT2S WT2S L 40 0 100 0 WT2S TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 9283 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0211 M CARGO TANK WT 2 S VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT2S WT2S WT2S WT2S WT2S WT2S WT2S BOTTOM VALVE CNTR BOTTOM VALVE PORT COW SUPPLY VALVE COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List 2 89 G00541 000540 01003261 000517 000543 000544 000533 000534 SUAS 000570 2 2 90 U00510 L00511 L00513 L00514 X00516 M00503 00502 00522 00523
99. 6 TANK VOLUME 30813 m3 C V00202 WTIS TANK VOLUME 12554 m3 D V00302 WTIP TANK VOLUME 12554 m3 E V00402 CT2 TANK VOLUME cap 30818 m3 F 00502 WT2S TANK VOLUME cap 9283 m3 G V00602 WT2P TANK VOLUME cap 9283 m3 H V00702 WT3BS TANK VOLUME cap 5231 m3 I V01002 WT3BP TANK VOLUME cap 5231 m3 J 1102 90 CT3 TANK VOLUME cap 30818 m3 1202 96 WT4S TANK VOLUME 14514 m3 L V01302 96 WT4P TANK VOLUME cap 14514 m3 M V01402 CT4 TANK VOLUME cap 30806 m3 01502 96 WT5S TANK VOLUME cap 8808 m3 V01602 5 TANK VOLUME 8808 m3 01702 WT6S TANK VOLUME cap 4024 m3 Q V02002 WT6P TANK VOLUME cap 4024 m3 R S V04110 FORE HFO TANK VOLUME T V04120 AFT HFO TANK VOLUME CHT2000 VLCC II ws Variable List Page 79 N 100153 100253 00353 00453 00553 100653 01153 01253 L T01353 M T01453 T01553 T01653 T01753 T02053 AS DOMME Q Z gt N M00105 M00205 M00305 M00405 M00505 M00605 M01105 M01205 M01305 M01405 M01505 M01605 M01705 M02005 Q Z O 2 O Z lt i R Page 80 Doc no SO 0604 A January 6 1997 Page 0504 M TANK SURVEY TEMPERATURES degC degC degC degC degC degC degC degC degC degC degC degC degC degC L 40 0 L 40 0 L 40 0 L 40 0 L 40 0 L 40 0 L 40 0
100. 6 24 L 0 23 CHT2000 ULCC II REU 1 3 The hullis deflection from the straight line is calculated from the bending moments and from the elasticity of each hull section The Deflection L in each section 0 12 is expressed in Metres Positive deflection represent a hogging hull condition negative deflection represent a sagging hull condition CHT2000 VLCC II ws User s Manual Page 4 48 Doc no SO 0603 A 9 January 1997 4 5 6 Stability Curve 00 07 00 Picture m Alarm Running 106 Stability Curve Group ONTRO HEEL CONDITION DEADWEIGHT DRAUGHT meter TRIH Ng u Sea Density 0 1025 0 1880 ton 180 80 Aft 1 18 51 3 Sea temp 25 00 C X of 36 1 Mid STBO L 18 30 4 summer mark Mid PORT L 18 30 DISPLACEMENT STABILITY meter Fud L 18 03 2 1000 ton 210 35 GM Corr 15 50 Trim E42 FS Heel 10 00 ed 10 72 86 00 50 00 OS Rad 14 91 5 Des Gz Angle of list degrees gt DEG 5 10 15 20 25 30 35 40 45 50 55 50 VALUE 0 48 18 97 1 47 11 83 12 03 12 15 2 18 12 15 2 06 11 87 11 65 1 47 CHT2000 ULCC II REV 1 3 The stability curve in the form of righting arm values is computed for heel angles ranging from 0 to 10 degrees From this the meta centric height is computed All righting arm values are corrected reduced for possible free surface effects The reduction in meta centric heights is
101. 7 X01230 T01253 HANAARHVOZ N um gt 1236 V01235 1264 ASS m Q a m g Q gt V01261 L V01262 M V01263 m EO Pee Doc no SO 0606 A January 6 1997 Page 0310 M CARGO TANK WT 4 S MAIN VARIABLES m m3 h m3 h bar degC L 0 5 25 0 WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S L 0 1 0 1 WT4S 1 0 0 H 8 0 WT4S WT4S L 40 0 H 100 0 WT4S TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 14514 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE 0311 M CARGO TANK WT 4 S VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT4S WT4S WT4S WT4S WT4S WT4S CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 57 N E 601241 G01240 001217 001243 001244 gt 001233 G01234 lt G01270 2 112 001210 101211 101213 101214 X01216 01203 V01202 M01222 M01223 M01224 M01225 M01207 M01206 M01215 D01220 D01221 Q Z O 2 O Z lt i R r Q m i 9 Q Z gt
102. 760 degC FPT BALLAST TEMPERATURE Load Master B T06761 degC CT1 CARGO TEMPERATURE Load Master C T06762 degC WT1S CARGO TEMPERATURE Load Master D T06763 degC WTIP CARGO TEMPERATURE Load Master E T06764 degC CT2 CARGO TEMPERATURE Load Master F T06765 degC WT2S CARGO TEMPERATURE Load Master G T06766 degC WT2P CARGO TEMPERATURE Load Master H T06767 degC WT3BS BALLAST TEMPERATURE Load Master I T06770 degC WT3BP BALLAST TEMPERATURE Load Master J T06771 degC CT3 CARGO TEMPERATURE Load Master K T06772 degC WT4S CARGO TEMPERATURE Load Master L T06773 degC WT4P CARGO TEMPERATURE Load Master M T06774 degC CT4 CARGO TEMPERATURE Load Master N T06775 degC WTSS CARGO TEMPERATURE Load Master O T06776 degC WTSP CARGO TEMPERATURE Load Master P T06777 degC WT6S SLOP TEMPERATURE Load Master Q T06780 degC WT6P SLOP TEMPERATURE Load Master R S T 2 172 Page 0704 M LOAD MASTER SOUNDINGS 06500 SOUNDING Load Master B L06501 m SOUNDING Load Master 106502 WTIS SOUNDING Load Master D L06503 WTIP SOUNDING Load Master E L06504 m CT2 SOUNDING Load Master F L06505 m WT2S SOUNDING Load Master G L06506 m WT2P SOUNDING Load Master H L06507 m WT3BS SOUNDING Load Master I L06510 m WT3BP SOUNDING Load Master J L06511 m CT3 SOUNDING Load Master K L06512 m WT4S SOUNDING Load Master L L06513 m WT4P SOUNDING Load Master M L06514 m
103. A 16 03 00 5 3 Cargo Handling Training from the Graphic Workstation When cargo handling training is done from the graphic workstation the description made for the VLCC II has to be supplemented by the correct mimic pictures The following picture directory is then to be used CHT2000 VLCC II ws User s Manual Page 5 21 Doc no SO 0603 A 16 03 00 5 3 1 Picture directory Slop Tanks Oil Discharge Crude Oil Pump 2 separator ccs go Diagram Monitor Pen Recorder 126 Wing Tank I PortCondition 127 Wing Tank 2 Port Condition 500 Directory 2 LOAD MASTER CHT2000 VLCC II ws User s Manual Page 5 22 Doc no SO 0603 A 16 03 00 5 3 2 Picture Directory 2 LOAD MASTER The following mimic pictures from the Load Master are available The operational description follows hereafter 501 Cargo Bargraph Load Master 50 Cargo Survey Load 503 Shear Force Load Master 504 Bending Moment Load Master 505 Deflection Load Master J 506 StabilityCurve Load J CHT2000 VLCC II ws User s Manual Page 5 23 Doc no SO 0603 A 16 03 00 Off line cargo calculation is entered through picture directory 2 Load Master A complete precalculation of trim stability and stress is conducted by entering the volume or Mass in each tank from the cargo bargraph picture By using the short cut button the variable page will
104. AIN 43 Page iii Doc no SO 0604 A January 6 1997 2 82 0201 M CARGO TANK CT 2 VALVES 43 2 83 Page 0202 M CARGO TANK CT 2 FLOWS 44 2 84 Page 0203 M CARGO TANK CT 2 LEVELS MASSES 44 2 85 Page 0204 M CARGO TANK CT 2 HEATING RN 45 2 86 Page 0205 M CARGO TANK CT 2 MISCELLANEOUS 45 2 87 Page 0210 M CARGO TANK WT 2 S MAIN VARIABLES 46 2 88 Page 0211 M CARGO TANK WT 2 S 46 2 89 Page 0212 M CARGO TANK WT 2 S FLOWS 47 2 90 Page 0213 M CARGO TANK WT 2 S LEVELS MASSES 47 2 9 Page 0214 M CARGO TANK WT 2 S 48 2 02 Page 0215 M CARGO TANK WT 2 S MISCELLANEOUS 48 2 93 Page 0220 M CARGO TANK WT 2 P MAIN VARIABLES 49 2 94 Page 0221 M CARGO TANK WT 2 P 49 2 05 Page 0222 M CARGO TANK WT 2 P FLOWS 50 2 96 Page 0223 M CARGO TANK WT 2 P LEVELS MASSES 50 2 97 Page 0224 M CARGO TANK WT 2 P 2 51 2 98 Page 0225 M CARGO TANK WT 2 P MISCELLANEOUS 5
105. ANK MASS incl residues TANK VOLUME cap 12554 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List 2 73 100253 V00256 G00257 E00260 E00254 E00255 HP Z Q m 9 Z Z r ATT m Q m m 9 Q Z gt 2 74 Z00272 P00226 X00227 X00230 M00231 m Q a a 2 Q Z gt P00245 00246 P00247 200268 200269 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0114 M CARGO TANK WT 1 S HEATING degC m3 h kW kW kW L 40 0 H 100 0 5 CARGO TEMPERATURE WT1S CARGO HEATING STEAM VALVE WTIS WTIS CARGO HEATING STEAM FLOW HEAT FROM STEAM WTIS HEAT LOSS TO SEA AIR WTIS HEAT LOSS TO ADJACENT TANKS Page 0115 M CARGO TANK WT 1 S MISCELLANEOUS 0 2 bar L 0 1 L 0 0 H 0 1 H 8 0 kg M00232 kg bar bar bar DEG DEG WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS WTIS IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 02 CO2 N2 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT Page 39 2 75 000312 100311 U00310 00302 00303 00305 000350 000367 Ja oe
106. ARBOARD cbal U25 28 U1 67 041 04 Ullage meter sloP 08 57 01 95 A 1 MT 5 WT 4S MT 3 S 138 12 135 E CHT2888 ULCC II REV 1 2 DEADWEIGHT 180 80 1000 36 17 Z of summer mark The Cargo Survey picture will give an overview of the ullage in the cargo ballast and HFO tanks Ship conditions will be dynamic updated based on tank ullage CHT2000 VLCC II ws User s Manual Page 4 44 4 5 3 Doc no SO 0603 A 9 January 1997 Shear Force 00 02 59 Picture Alarm NOR Running 103 Shear Force Group ON HEEL CONDITION DEADWEIGHT DRAUGHT meter TRIN Mg 4 Sea Density D 1025 0 1888 ton H 180 80 Aft 1 18 51 i 3 Sea temp 25 00 X of V 96 17 Mid STBD L 18 30 4 2 summer mark Mid PORT L 18 30 9H rr DISPLACEMENT STABILITY meter Fud L 18 03 548 1888 ton 210 35 GM Corr 15 56 Trim pou E w FS Red 19 72 1 10 00 X0 00 05 Rad 14 91 X0 08 Limits Harbour pen sea 10 P 5 H P 1 83 R 2 8 A P0 37 A P7 46 A tonnes P 5 88 A P 3 42 A 5 A P 2 43 8 P3 04 P8 09 A CHT2000 VLCC II ws User s Manual CHT2888 ULCC II 1 3 Page 4 45 Doc no SO 0603 A 9 January 1997 The Shear Forces are calculated from the load distribution of the ship including the steel weights of the different hull sectio
107. AUTO mode Page 5 96 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 This page is intentionally left blank Page 5 97 Doc no SO 0603 A 16 03 00 01 41 14 Picture Alarm Running ND 210 Inert Gas Distribution Group ork 1 1 1 1 M V M M I 68 08 8889 16 68 08 1 68 08 6738 13 TE PEU 2 1 J 1 1 125 124 123 122 otk 4 oy 1 ok IE cT 4 CT 2 cT 1 1 1 1 l i 1 1 1 1 V 1 V V V 1 A A 61874 4 68 08 G 88 18 61580 7 EET 5 basl1ast 209 1 1 gt 1 1 1 1 1 1 11 1 1 1 1 d 1 I 68 08 6892 11 68 08 68 08 6724 94 M M M M 1 D D D CHT2000 ULCC II REV 1 1 CHT2000 VLCC II ws User s Manual Page 5 98 Doc no SO 0603 A 16 03 00 5 8 5 Distribution The Inert Gas can be distributed to the various tanks by operating the isolation valves These valves are simulated by clicking on the Inert Gas Distribution picture MD 210 An illuminated symbol indicates an open valve These valves can also be operated from the Tank condition pictures MD 122 135 5 8 6 Tank Atmosphere Pressure Control The gas pressure in the tanks is normally regulated by the automatic Pressure Vacuum Valves An open valve is indicate
108. BINE 7 Page 0012 M CARGO LINE 1 PUMP BEARING CONTROL 7 Page 0013 M CARGO LINE 1 VACUUM 8 Page 0014 M CARGO LINE 1 BOTTOM PI PING 8 Page 0015 M CARGO LINE 1 DECK PIPING 9 Page 0016 M CARGO LINE 1 PUMP MONITOR PAGE 9 Page 0017 M CARGO LINE 1 PUMP DESIGN DATA 10 0020 M CARGO LIME 2 VALVES 10 Page 0021 M CARGO LINE 2 PUMP TURBINE 11 Page 0022 M CARGO LINE 2 PUMP BEARING CONTROL 11 Page 0023 M CARGO LINE 2 VACUUM 12 Page 0024 M CARGO LINE 2 BOTTOM PIPING 12 Page 0025 M CARGO LINE 2 DECK PIPING 13 Page 0026 M CARGO LINE 2 PUMP MONITOR 13 Page 0027 M CARGO LINE 2 PUMP DESIGN DATA 14 0030 M CARGO LINE 3 VALVES 14 Page 0031 M CARGO LINE 3 PUMP TURBINE 15 Page 0032 M CARGO LINE 3 PUMP BEARING CONTROL 15 Page 0033 M CARGO LINE 3 VACUUM
109. CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT Page 51 2 99 mask amin lt zd N V00735 G00740 G00717 deomovoz 2 100 A B T00753 C D E00754 E E00755 a de mWovozzcm mo Page 52 Doc no SO 0604 A January 6 1997 Page 0230 M BALLAST TANK WT 3 S MAIN VARIABLES m L 0 5 250 WT3BS TANK ULLAGE measured WT3BS SOUNDING even keel WT3BS TANK ULLAGE even keel WT3BS TANK VOLUME cap 5231 m3 B B tonn WT3BS CLEAN WATER MASS WT3BS BOTTOM VALVE m3 h WT3BS BOTTOM OUTLET FLOW m3 s 100 H 1 0 WT3BS TANK TOP OVERFLOW Page 0231 M BALLAST TANK WT 3 S MISCELLANEOUS degC 1 40 0 H 100 0 WT3BS TEMPERATURE kW WT3BS HEAT LOSS TO SEA AIR kW WT3BS HEAT LOSS TO ADJACENT TANKS bar WT3BS LIQUID GAS PRESSURE bar WT3BS GEODETIC PRESSURE bar WT3BS TOTAL TANK BOTTOM PRESSURE kg m3 WT3BS WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List 2 101 A B U01012 D L01011 F 901010 01002 I M01025 V01035 001040 901017 2 102 1053 D 1054 E E01055 F G H 1045 I 01046 J P01047 K 1 201021 Pere Ven S CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0240 M BALLAST TANK WT 3 P MAIN VARIABLES m L 0 5 25 0 m m tonn m3 h m3 s L 0 0 H 1 0
110. CC II ws Alarm List Page 7 ve 2 10 gos X03247 E N03110 F P03115 Z03107 T 03241 J T03242 5 Page 8 Doc no SO 0604 A January 6 1997 Page 1000 AG10 CARGO PUMP 4 SYSTEM 1 1 0 5 L 0 0 1 0 COP4 TRIP INDICATION rpm L 0 0 Hz1950 0 COP4 SPEED bar 1 00 H 20 0 COP4 DISCHARGE PRESS before choke L 0 0 400 COP4 CAVITATION INDEX bar 1 10 H 5 0 COP4 BEARING LO PRESSURE degC Lz0 0 70 0 BEARING TEMPERATURE m L 1 0 H 5 0 COP4 SEPARATOR LEVEL Page 1100 AG11 BALLAST PUMP SYSTEM 1 1 0 5 L 0 0 H 1 0 BWP TRIP INDICATION rpm L 0 0 H 1950 0 BWP SPEED bar 1 00 200 BWP DISCHARGE PRESS before choke 1 00 H 40 0 BWP CAVITATION INDEX bar 1 10 H 5 0 BWP BEARING LO PRESSURE degC L 0 0 H 70 0 BWP BEARING TEMPERATURE CHT2000 VLCC II ws Alarm List 2 11 006021 006022 006023 006024 006025 006026 006027 1 006030 J 006031 006032 L 006033 Q m m go gt X07021 39290 2 12 P06001 P06002 P06003 P06004 P06005 P06006 P06007 P06010 P06011 P06012 P06013 Z r m Q m m 9 Q Z gt 32 OO Oo Doc no SO 0604 A January 6 1997 71300 AG13 HULL BENDING MOMENTS 1 1 ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm lt 0 1 gt L 0 0 Page 1400 AG14 HULL SHEAR FORCES 1 1 ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn kt
111. CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 30818 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC Page 55 Doc no SO 0604 A January 6 1997 2 107 0304 M CARGO TANK CT 3 HEATING A B C 01153 degC 1 40 0 H 100 0 CT3 CARGO TEMPERATURE E 1156 96 CT3 CARGO HEATING STEAM VALVE 001157 m3 h CT3 CARGO HEATING STEAM FLOW H I 01160 kW CT3 HEAT FROM STEAM J 01154 kW CT3 HEAT LOSS TO SEA AIR K E01155 kW CT3 HEAT LOSS TO ADJACENT TANKS L M N O P Q R S T 2 108 Page 0305 M CARGO TANK CT 3 MISCELLANEOUS A 701172 lt 0 2 gt CT3 IG INITIATION 1 air 2 IG C D E 01126 bar L 0 1 H 0 1 CT3 TANK ATMOSPHERIC PRESSURE F X01127 96 L 0 0 8 0 CT3 OXYGEN CONTENT G X01130 CT3 HYDRO CARBON CONTENT H M01131 CT3 INERT GAS MASS 02 CO2 N2 J M01132 kg CT3 HYDRO CARBON MASS K L P01145 bar CT3 LIQUID GAS PRESSURE M P01146 bar CT3 GEODETIC PRESSURE N P01147 bar CT3 TOTAL TANK BOTTOM PRESSURE O P 701168 DEG CT3 TANK CLEANING UPPER LIMIT 701169 DEG CT3 TANK CLEANING LOWER LIMIT R S T Page 56 CHT2000 VLCC II ws Variable List N E gt og U01212 L01211 U01210 V01202 V01201 01203 01205 001250 lt t m Q 1 m G01267 P01226 X0122
112. CT4 SOUNDING Load Master N L06515 m WT5S SOUNDING Load Master O L06516 m WTSP SOUNDING Load Master P L06517 m WT6S SOUNDING Load Master Q L06520 m WT6P SOUNDING Load Master R L06521 m FHFO SOUNDING Load Master S L06522 m AHFO SOUNDING Load Master T Page 88 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 173 A U06530 m L 0 0 H 0 0 B U06531 m L 0 0 0 0 C U06532 m L 0 0 0 0 D 006533 m L 0 0 0 0 E U06534 m L 0 0 0 0 F U06535 m L 0 0 0 0 006536 m L 0 0 0 0 H U06537 m L 0 0 0 0 I U06540 m L 0 0 0 0 J U06541 m L 0 0 0 0 K U06542 m L 0 0 H 0 0 L U06543 m L 0 0 0 0 M U06544 L 0 0 0 0 N U06545 m L 0 0 0 0 O U06546 m L 0 0 H 0 0 P U06547 m L 0 0 0 0 Q U06550 m L 0 0 0 0 R U06551 m L 0 0 0 0 S U06552 m L 0 0 0 0 T 2 174 A M06560 tonn B M06561 tonn C M06562 tonn D M06563 E M06564 tonn F M06565 tonn G M06566 tonn H M06567 tonn I M06570 tonn J M06571 tonn K M06572 tonn L M06573 tonn M M06574 tonn N M06575 tonn O M06576 tonn P M06577 tonn Q M06600 tonn R M06601 tonn S M06602 tonn T CHT2000 VLCC II ws Variable List Page 0705 M LOAD MASTER ULLAGES FPT TANK ULLAGE Load Master CTI TANK ULLAGE Load Master WTIS TANK ULLAGE Load Master WTIP TANK ULLAGE Load Master CT2 TANK ULLAGE Load Master WT2S TANK ULLAGE Load Master WT2P TANK ULLAGE Load
113. D and its corresponding number in word Enter MD and the MD s number without space 1 MD 101 and Enter Previous Picture Next Picture Allows scrolling to next previous model drawing ex MD 07 MD 08 and MD 09 in line as listed in picture directory Alarm Acknowledge Acknowledges the alarm being pointed at with the cursor Use either the Acknowledge button at the Operator panel or the left tracker ball button Alarm Log Displays pages of all present alarms To acknowledge all alarms in that specific page press EXTENDED CHAR button and A simultaneously Press the NEXT or PREV key at the HP keyboard to get the next page of alarms Alarm Silence Resets alarm horn where installed in the Cargo Control Room and the internal buzzer in the TEC2000 keyboard Page 5 19 5 2 3 11 5 2 3 12 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Print Report The Print report field is on the lower part of the VDU and by pressing this soft button a complete printout of the alarm status is initiated Unit Conversion The Unit Conversion field is on the lower part of the VDU and by pressing this soft button a menu of different conversions pops up Length Volume Area etc Press one of the softkeys in the menu Press the middle button on the tracker ball and type the value of the specific unit you want to be converted And read the converted values in the other fields Page 5 20 Doc no SO 0603
114. Doc no SO 0603 A 9 January 1997 Cargo Handling Trainer CHT2000 VLCC II ws USER S MANUAL Department Author Approved by Aksel D Nordholm Harald Kluken 2000 KONGSBERG NORCONTROL AS All rights reserved No part of this work covered by the copyright hereon may be reproduced or otherwise copied without prior permission from KONGSBERG NORCONTROL AS CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 9 January 1997 DOCUMENT STATUS SO 0603 A 9 January 1997 ADN td CHANGES IN DOCUMENT Paragraph Paragraph Heading No Description of Change First issue CHT2000 VLCC II ws User s Manual Page i Doc no SO 0603 A 9 January 1997 Section 1 1 1 1 2 1 3 1 4 2 2 1 2 2 3 3 1 3 2 3 3 3 4 4 4 1 4 2 4 2 1 4 2 2 4 3 4 4 4 5 4 5 1 4 5 2 4 5 3 4 5 4 4 5 5 4 5 6 4 5 7 4 5 8 4 5 9 4 5 10 4 5 11 4 5 12 4 5 13 4 5 14 4 5 15 4 5 16 4 5 17 TABLE OF CONTENTS Page INTRODUCTION 1 1 Concept Description 1 2 system 1 cease 1 3 Simulator Configuratig nt 1 4 Simulator Concept a 1 5 TECHNICAL SPECIFICATION Eit cei pup n DE 2 1 Workstation HP 9000 425e a 2 1 Server HP C 3020 2 1 INSTALLATION 3 1 Introduction
115. E CONSTANT 3 0020 M CARGO LINE 2 VALVES lt 0 1 gt MANIFOLD 2 SHUT OFF VALVE stbd lt 0 1 gt MANIFOLD 2 SHUT OFF VALVE port lt 0 1 gt MANIFOLD 2 DRAIN VALVE DECK LINE 2 SHUT OFF VALVE lt 0 1 gt LOAD LINE 2 SHUT OFF VALVE lt 0 1 gt TC COW CROSSOVER VALVE lt 0 1 gt SLOP CROSSOVER VALVE lt 0 1 gt CO SUCTION CROSSOVER VALVE lt 0 1 gt SW SUCTION CROSSOVER VALVE lt 0 1 gt BOTTOM LINE 2 SHUT OFF VALVE lt 0 1 gt BOTTOM LINE 2 3 CONNECTION VALVE CHT2000 VLCC II ws Variable List 2 17 02312 2313 002314 2315 2316 2322 02310 N02301 E02320 702321 202307 SOAS ROMO m gt V02303 002306 002304 202305 2 18 2441 T02442 g Q gt tri V02311 R02440 R02446 X02447 02333 R02334 02300 02466 3JONOUOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0021 M CARGO LINE 2 PUMP TURBINE m3 h bar bar bar L 0 0 rpm L 0 0 rpm kW L 0 0 m3 h kWh kg H 20 0 COP2 DISCHARGE VALVE POS COP2 DISCHARGE VALVE POS COMMAND COP2 FLOW COP2 DISCHARGE PRESS before choke COP2 DISCHARGE PRESS after choke COP2 SUCTION PRESSURE H 1950 0 COP2 SPEED H 40 0 COP2 SPEED COMMAND COP2 POWER COP2 HYDRAULIC EFFICIENCY COP2 CAVITATION INDEX COP2 TURBINE STEAM CONTROL VALVE POS COP2 TURBINE SHAFT TORQUE TURBINE STEAM F
116. GE PRESS before choke BWP DISCHARGE PRESS after choke BWP SUCTION PRESSURE H 1950 0 BWP SPEED H 40 0 BWP SPEED COMMAND BWP POWER BWP HYDRAULIC EFFICIENCY BWP CAVITATION INDEX BWP TURBINE STEAM CONTROL VALVE POS BWP TURBINE SHAFT TORQUE TURBINE STEAM FLOW BWP BWP TURBINE EFFICIENCY Page 0052 BALLAST WATER LINE PUMP BEARING CONTROL bar L 1 0 degC L 0 0 lt 0 1 gt lt 0 1 gt 0 5 L 0 0 5 0 H 70 0 H 1 0 BWP BEARING LO PRESSURE BWP BEARING TEMPERATURE BWP RECIRCULATION VALVE POS BWP LUB OIL PUMP START BWP START STOP BWP TRIP INDICATION BWP GOVERNOR GAIN CONSTANT BWP GOVERNOR RESET TIME CONSTANT Page 23 Doc no SO 0604 A January 6 1997 2 43 0053 M BALLAST WATER LINE FLOWS A G03200 m3 h FLOW FROM FPEAK TANK 603201 m3 h FLOW FROM TANK WT 3 S 603202 m3 h FLOW FROM TANK WT 3 P D 603170 m3 h BW SEA CHEST INLET FLOW F G03171 m3 h SUCTION FLOW FROM BW SEA CHEST LINE 603172 m3 h SUCTION FLOW FROM BW BOTTOM LINE H I G03161 m3 h DISCHARGE FLOW TO BW SEA CHEST LINE J G03160 m3 h DISCHARGE FLOW TO BW BOTTOM LINE 03162 DISCHARGE FLOW TO BW DECK LINE L M G03260 m3 h BW DROP FLOW INTO TANK CT2 N G03261 m3 h BW DROP FLOW INTO TANK WT2S O G03262 m3 h BW DROP FLOW INTO TANK WT2P P Q G03263 m3 h BW DROP FLOW INTO TANK CT4 R G03264 m3 h BW DROP FLOW INTO TANK WT5S G03265 m3 h BW DROP FLOW INTO
117. H 06753 96 FW LO VOLUME Load Master I J M06601 tonn FHFO TANK MASS Load Master L M06602 tonn AHFO TANK MASS Load Master 06605 tonn SETTLING TANK MASS Load Master M06606 tonn SERVICE TANK MASS _ Load Master O M06607 tonn DO STORAGE TANK MASS Load Master P M06608 tonn DO SETTLING TANK MASS Load Master M06609 tonn DO SERVICE TANK MASS Load Master R M06603 tonn FW LO MASS Load Master S T 2 176 Page 0708 M LOAD MASTER DRAFT A B C L04020 m MEAN DRAFT Load Master D L04021 m HULL TRIM Load Master E L04022 m HULL HEEL Load Master F G H Z04031 DEADWEIGHT relative Load Master M04030 ktonn DEADWEIGHT Load Master J K M04032 ktonn DISPLACEMENT Load Master L M N O P Q R S T Page 90 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 177 Page 0710 M LOAD MASTER HULL SHEAR FORCES A 06400 L 20 0 H 20 0 SHEAR FORCE section 0 LM P06401 L 16 0 H 16 0 SHEAR FORCE section 1 LM D 06402 ktonn L 18 0 H 18 0 SHEAR FORCE section 2 LM P06403 L 20 0 H 20 0 SHEAR FORCE section 3 LM F 06404 L 18 0 H 18 0 SHEAR FORCE section 4 LM P06405 ktonn L 16 0 H 16 0 SHEAR FORCE section 5 LM 06406 ktonn L 16 0 H 16 0 SHEAR FORCE section 6 LM I P06407 ktonn L 18 0 H 18 0 SHEAR FORCE section 7 LM J 410
118. HERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE 0201 M CARGO TANK CT 2 VALVES 0 1 96 lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt CT2 CT2 CT2 CT2 CT2 CT2 CT2 CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE STBD BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 43 2 83 G00441 G00442 G00440 G03260 G00417 G00443 G00444 G00433 000434 ZU ASO ROM OO 000470 2 84 000410 1 00411 L00413 L00414 X00416 M00403 V00402 M00422 M00423 M00424 M00425 M00407 M00406 M00415 D00420 D00421 Z O 2 O Z lt 2 AST r Q m m 9 Q Z gt Page 44 Doc no SO 0604 A January 6 1997 Page 0202 M CARGO TANK CT 2 FLOWS m3 h m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 CT2 CT2 CT2 BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION BOTTOM OUTLET FLOW PORT SUCTION BW DROP FLOW INTO TANK CT2 CT2 CT2 CT2 CT2 CT2 CT2 TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0203 M CARGO TANK 2 LEVELS MASSES m m m m CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 CT2 TANK ULLAGE even kee
119. HT2000 ULCC II REV 1 1 The fresh water tank and the DO HFO tanks are auxiliary tanks that can filled emptied directly from this picture by changing the volume variable Variable page 0074 Consumption of on the boiler will be from tank aft which reflect the transfer to the aux tanks During sea voyage one must transfer HFO from HFO tank fore by starting the transfer pump Variable page 0073 CHT2000 VLCC II ws User s Manual Page 4 59 Doc no SO 0603 A 9 January 1997 4 5 21 Loading Discharge Ballast Routing HD 206 Load Discharge Ballast Routing trae NOR 188 187 ioe 4 mm XXX XX DE HLI 29 pa Bia Bia oe E Ballast_line ep TI a x re H Loading Discharging Ballasting Routing picture shows operator how pipelines are routed from manifolds and sea chests into the cargo and ballast tanks This picture is not dynamically updated CHT2000 VLCC II ws User s Manual CHT2000 ULCC II REV 1 2 Page 4 60 Doc no SO 0603 A 9 January 1997 4 5 22 Monitor 01 36 48 Picture Alarm NOR Running MD 207 Monitor
120. I ws User s Manual Page 1 1 Doc no SO 0603 A 9 January 1997 1 1 Concept Description The CHT2000 VLCC II ws is based on the simulator design and development system Operator Training Simulation System OTISS developed by Special Analysis and Simulation Technology Ltd SAST UK The Operator Man Machine Interface MMI is realised using the EMULA Graphic software Package developed by Institutt For Energiteknikk IFE Halden Norway The CHT2000 VLCC II ws system is implemented on a network of Hewlett Packard 9000 series computers The structure of the system is outlined in the following illustration By the simulation of faults and deterioration s the instructor can create a training situations that enables the trainee to meet and overcome these problems This training environment will give the students experience in dealing with problems that would normally demand years of seagoing experience The third part of the simulator is the instructor s station which includes the simulator controls for Changing operational and ambient conditions Setting faults and deterioration s single or in series Simulate leaks in cargo lines and tank bulkheads Resetting faults Logging events and alarms General system communication The CHT2000 VLCC II ws is designed to train students in cargo handling operation under both normal and abnormal conditions It is therefore of utmost importance that the training takes place in a
121. International and National Rules and Regulations the demand for more safe cargo handling has increased At the same time new technology has made more advanced training simulators available at an affordable price The purpose of Kongsberg Norcontrol s Cargo Handling Trainer CHT2000 VLCC II ws is to provide an educational tool that gives a realistic reproduction of the dynamic behaviour of a typical WLCC cargo handling system and reflects the interactions between the different auxiliary systems A well designed computerised simulator will to a great extent give the same training facilities which means training in the normal operation of a ship s cargo handling system In addition to giving the students operational training CHT2000 VLCC II ws is also tool for more intimate theoretical studies for loading discharging operations such as Planning the operations by using CHT2000 VLCC II ws as a load computer Run test conditions on the loading computer Studying single components Studying tank atmosphere Studying inert gas in relation to boiler load Monitoring the discharge cost and time Provide training in operations that the officers will have benefit of later on Shows you the results of incorrect operations without damaging the equipment Presents all relevant terminology and relates it to associated hardware Demonstrates both theoretical aspects and practical results in one and the same room CHT2000 VLCC I
122. LLAGE even keel 000610 WT2P TANK even keel H U00710 m WT3BS TANK ULLAGE even keel I 001010 WT3P TANK ULLAGE even keel J U01110 m CT3 TANK ULLAGE even keel K U01210 m WT4S TANK ULLAGE even keel L U01310 m WT4P TANK ULLAGE even keel M U01410 m CT4 TANK ULLAGE even keel N U01510 m WTSS TANK ULLAGE even keel O U01610 m WTSP TANK ULLAGE even keel P U01710 m WT6S TANK ULLAGE even keel Q U02010 m WT6P TANK ULLAGE even keel R 5 2 158 Page 0507 M TANK SURVEY ULLAGES mes 000012 L 0 5 25 0 TANK ULLAGE measured 000112 m L 0 5 25 0 TANK ULLAGE measured 000212 L 0 5 25 0 WTIS TANK ULLAGE measured D U00312 m L 0 5 H 25 0 TANK ULLAGE measured E U00412 m L 0 5 H 25 0 CT2 TANK ULLAGE measured 900512 L 0 5 H 25 0 WT2S TANK ULLAGE measured 000612 1 05 H 25 0 WT2P TANK ULLAGE measured H U00712 m L 0 5 H 25 0 WT3BS TANK ULLAGE measured I U01012 m L 0 5 H 25 0 WT3P TANK ULLAGE measured J 001112 m L 0 5 25 0 CT3 TANK ULLAGE measured K U01212 m L 0 5 H 25 0 WT4S TANK ULLAGE measured L U01312 m L 0 5 H 25 0 WT4P TANK ULLAGE measured M U01412 m L 0 5 H 25 0 CT4 TANK ULLAGE measured 001512 m L 0 5 H 25 0 WTSS TANK ULLAGE measured 001612 m L 0 5 H 25 0 WTSP TANK ULLAGE measured P 001712 m L 05 25 0 WT6S TANK ULLAGE measured Q U02012 m L 05 H 25 0 WT6P TANK ULLAGE meas
123. LLANEOUS 0 1 Plug in BALANCE line 0 1 Plug in EQUALIZING line 0 100 SWSC sea chest inlet STBD dirty 0 100 SWSC sea chest inlet PORT dirty 0 100 Ballast sea chest inlet dirty 0 1 Hydraulic supply failure CHT2000 VLCC II ws Malfunction List Page 9 Doc no SO 0603 A 6 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Appendix D Variable List Doc no SO 0606 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 6 January 1997 4 APPENDIX D VARIABLE LIST CHT2000 VLCC II ws User s Manual H Section 1 2 2 1 2 2 2 3 2 4 2 5 2 6 2 7 2 8 2 9 2 10 2 11 2 12 2 13 2 14 2 15 2 16 2 17 2 18 2 19 2 20 2 2 2 22 2 23 2 24 2 25 2 26 2 27 2 28 2 29 2 30 2 31 2 32 2 33 2 34 2 35 2 36 2 37 Page Doc no SO 0604 A January 6 1997 TABLE OF CONTENTS Page DIRECTORY EIS Teea teach 1 VARIABLE LIST e e emen nnn enn 3 Page 0002 M SIMULATOR TIME CONTROL 3 P sge 0003 Me SEA SHIP STATE 3 Page 0004 M SHORE CONNECTION DATA 4 Page 0005 M MANIFOLD VALVES AND FLOWS 4 Page 0006 M MANIFOLD MONITOR RN 5 Pace 0007 M POLLUTION MONITOR RN 5 Page 0008 M PUMP WORK MONITOR Nt 6 Page 0010 M CARGO LINE 1 VALVES Nt 6 Page 0011 M CARGO LINE 1 PUMP TUR
124. LOW COP2 COP2 TURBINE EFFICIENCY Page 0022 M CARGO LINE 2 PUMP BEARING CONTROL bar L 1 0 degC L 0 0 lt 0 1 gt lt 0 1 gt lt 0 5 gt L 0 0 lt 0 1 gt lt 0 1 gt 5 0 H 70 0 H 1 0 COP2 BEARING LO PRESSURE COP2 BEARING TEMPERATURE COP2 RECIRCULATION VALVE POS COP2 LUB OIL PUMP START COP2 START STOP COP2 TRIP INDICATION COP2 SPEED SURGE CONTROL AUTO SWITCH COP2 FLOW SURGE CONTROL AUTO SWITCH COP2 GOVERNOR GAIN CONSTANT COP2 GOVERNOR RESET TIME CONSTANT Page 11 2 19 2335 RO2336 L02332 2330 002327 002325 002326 002371 002372 002370 Vn m i a urin a n aus X02324 2 20 002371 002370 002372 002400 002401 002410 002411 2373 2374 02375 F Pt r r Q m P J Q Z gt P02403 T02404 X02405 ARANHVOZ Page 12 Doc no SO 0604 A January 6 1997 0023 M CARGO LINE 2 VACUUM SEPARATOR lt 0 1 gt lt 0 1 gt m bar m3 h m3 h m3 h m3 h m3 h m3 h L 1 0 H 5 0 COP2 VACUUM PUMP START COP2 VACUUM PUMP AUTO SWITCH COP2 SEPARATOR LEVEL COP2 SEPARATOR GAS PRESSURE abs COP2 SEPARATOR INLET LIQUID FLOW COP2 SEPARATOR GAS INFLUX COP2 VACUUM PUMP GAS FLOW FLOW FROM BOTTOM LINE 2 FLOW FROM CO SUCTION CROSSOVER FLOW FROM SW SUCTION CROSSOVER COP2 SEPARATOR OIL CONTENT Page 0024 M CARGO LINE 2 BOTTOM PIPING m3 h m3 h m3 h m3 h m3 h m3
125. LOWER LIMIT CHT2000 VLCC II ws Variable List N N og U01412 L01411 U01410 V01402 V01401 01403 01405 001450 lt m Q 1 m G01467 P01426 X01427 X01430 01453 HaAROVOZ N N N V01436 V01435 V01437 m Q m m 2 Q gt V01464 m b lt ON L V01462 M V01463 We AO ros Doc no SO 0606 A January 6 1997 Page 0400 M CARGO TANK CT 4 MAIN VARIABLES m m3 h m3 h bar degC L 0 5 H 25 0 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CT4 0 1 H 0 1 CT4 L 0 0 H 8 0 CT4 CT4 L 40 0 H 100 0 CT4 TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 30806 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0401 M CARGO TANK CT 4 VALVES lt 0 1 gt 96 0 1 0 1 0 1 0 1 CT4 CT4 CT4 CT4 CT4 CT4 CT4 CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE PORT BOTTOM VALVE STBD COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 63 N N 9 001441 001440 001442 003263 001417 001443 001444 001433 001434 SUAS ODOM OO gt 601470
126. M COP3 TO SLOP CROSSOVER E F 002541 m3 h LOAD FLOW to bottom line 3 002543 m3 h FLOW FROM SHORE MANIFOLD 3 H I 2546 bar DECK LINE 3 PRESSURE aft J T02547 degC DECK LINE 2 TEMPERATURE K X02550 DECK LINE 3 OIL CONTENT aft L 2551 MANIFOLD 3 PRESSURE N T02552 degC MANIFOLD 2 TEMPERATURE 02553 MANIFOLD 3 OIL CONTENT P 002554 kg m3 MANIFOLD OIL DENSITY Q R 5 2 30 Page 0036 M CARGO LINE 3 PUMP MONITOR PAGE A B C T03750 hour TOTAL PUMP RUNNING TIME D M03751 ktonn TOTAL PUMP FLOW MASS E E03752 MWh TOTAL COP3 ENERGY F G H M03753 tonn TOTAL TURBINE STEAM MASS I Z03754 US TOTAL STEAM COST J K L 5 CHT2000 VLCC II ws Variable List Page 17 2 31 C02660 C02661 C02662 C02663 C02664 C02665 AP POVOZEU ATE m Q T Pi Z Q Z gt 2 32 V12762 V12763 m Q m gt V02764 V03025 V03026 m Q m V03022 L V03023 M V03020 V03021 V03024 Page 18 Doc no SO 0604 A January 6 1997 0037 M CARGO LINE 3 PUMP DESIGN DATA COP3 PRESS CONSTANT 1 COP3 PRESS CONSTANT 2 i COP3 PRESS CONSTANT 3 COP3 TORQUE CONSTANT 1 COP3 TORQUE CONSTANT 2 COP3 TORQUE CONSTANT 3 Page 0040 M CARGO LINE 4 VALVES lt 0 1 gt MANIFOLD 4 SHUT OFF VALVE stbd lt 0 1 gt MANIFOLD 4 SHUT OFF VALVE port lt 0 1 gt MANIFOLD 4 D
127. M1310 demovozztm momsmuow 2 11 A M1401 B M1402 C M1403 lt A co E r Q m Page 8 Doc no SO 0604 A January 6 1997 Page 1100 MA11 CARGO PUMP 3 4 0 100 Cargo pump 3 wear 0 100 Cargo pump 3 LO filter dirty 0 100 Cargo pump 3 turbine wear 0 100 Cargo pump 3 governor unstable 0 100 Cargo pump 4 wear 0 100 Cargo pump 4 LO filter dirty 0 100 Cargo pump 4 turbine wear 0 100 Cargo pump 4 governor unstable Page 1200 MA12 BALLAST PUMP 0 100 0 100 0 100 0 100 Ballast pump wear Ballast pump LO filter dirty Ballast pump turbine wear Ballast pump governor unstable ccc CHT2000 VLCC II ws Malfunction List 2 12 M1501 M1502 M1503 M1504 M1505 M1506 M1507 M1510 M1511 M1512 M1513 M1514 1515 M1516 AY RON 9 Z Z T AS m Q m F 9 Q Z p 2 13 A M1601 B M1602 C M1603 D M1604 E M1605 F M1606 Doc no SO 0605 A January 6 1997 Page 1300 MA13 INERT GAS SYSTEM 0 100 CT1 P V valve leakage 0 100 WT1S P V valve leakage 0 100 WTIP P V valve leakage 0 100 CT2 P V valve leakage 0 100 WT2S P V valve leakage 0 100 WT2P P V valve leakage 0 100 CT3 P V valve leakage 0 100 WT3BS P V valve leakage 0 100 WT3BP P V valve leakage 0 100 CT4 P V valve leakage 0 100 WT5S P V valve leakage 0 100 WTSP P V valve leakage 0 100 WT6S P V valve leakage 0 100 WT6P P V valve leakage Page 1400 MA14 MISCE
128. N 1 air 2 IG C D P00126 40 1 0 1 TANK ATMOSPHERIC PRESSURE F X00127 L 0 0 H 8 0 OXYGEN CONTENT G X00130 HYDRO CARBON CONTENT H 00131 INERT GAS MASS 02 CO2 N2 J 00132 kg HYDRO CARBON MASS K L P00145 bar LIQUID GAS PRESSURE 146 bar GEODETIC PRESSURE N P00147 bar TOTAL TANK BOTTOM PRESSURE O P Z00168 DEG CT1 TANK CLEANING UPPER LIMIT Q Z00169 DEG TANK CLEANING LOWER LIMIT R S T Page 36 CHT2000 VLCC II ws Variable List 2 69 og U00212 L00211 U00210 V00202 V00201 M00203 M00205 G00250 lt t m Q 1 m G00267 P00226 X00227 X00230 T00253 HANAAHVOZ 2 70 0236 00235 00264 8 r Q a m g Q gt V00261 L V00262 M V00263 m EO Yu Doc no SO 0606 A January 6 1997 Page 0110 M CARGO TANK WT 1 S MAIN VARIABLES m m3 h m3 h bar degC 0 5 25 0 WTIS WTIS WTIS WTIS WTIS WTIS WTIS 15 15 0 1 0 1 15 1 0 0 H 8 0 WTIS WTIS L 40 0 100 0 WTIS TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 12554 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE
129. ND C D 03634 tonn TOTAL TANK OVERFLOW MASS 03626 tonn TOTAL MANIFOLD SPILL OIL M03603 kg TOTAL OVER BOARD DISCHARGED OIL MASS H M03632 kg TOTAL IG DISCHARGE MASS J M03633 kg TOTAL HC DISCHARGE MASS K L M N O P Q R S E CHT2000 VLCC II ws Variable List Page 5 gt X03720 X03721 lt 03722 03723 TAMY 03724 703725 ee AO TOAS 52 gt V12162 V12163 V02166 V02164 V02225 V02226 gt 2222 M V02223 N V02220 O V02221 2224 R V02227 S V02228 T Page 6 Doc no SO 0604 A January 6 1997 0008 M PUMP WORK MONITOR lt 0 1 gt PUMP MONITOR ACTIVE lt 0 1 gt PUMP MONITOR RESET COMMAND ktonn TOTAL PUMP 1 5 FLOW MASS MWh TOTAL PUMP 1 5 ENERGY tonn TOTAL TURBINE 1 5 STEAM MASS US TOTAL TURBINE 1 5 STEAM COST Page 0010 M CARGO LINE 1 VALVES lt 0 1 gt MANIFOLD 1 SHUT OFF VALVE stbd lt 0 1 gt MANIFOLD 1 SHUT OFF VALVE port lt 0 1 gt MANIF 1 2 CROSSOVER VALVE lt 0 1 gt MANIFOLD 1 DRAIN VALVE DECK LINE 1 SHUT OFF VALVE lt 0 1 gt LOAD LINE 1 SHUT OFF VALVE lt 0 1 gt TC COW CROSSOVER VALVE lt 0 1 gt SLOP CROSSOVER VALVE lt 0 1 gt CO SUCTION CROSSOVER VALVE lt 0 1 gt SW SUCTION CROSSOVER VALVE lt 0 1 gt BOTTOM LINE 1 SHUT OFF VALVE lt 0 1 gt BOTTOM LINE 1 2 CONNECTION VALVE lt 0 1 gt BOTTOM LINE 1 2 CONNEC
130. O 0603 A 16 03 00 A scenario is a predefined list of actions and or malfunctions that will take place during the simulation when Running is activated Almost any action and malfunction available in the simulator can be included in a scenario The scenario push button when activated displays a directory of the scenarios already created This feature allows the instructor to load an already existing scenario or creating a new one Scenario To create a scenario enter scenario by pressing SCENARIO button Prompts on the screen will guide you through the preparation required Point and click the software button CREATE at the lower part of the screen and then point and click at the position where to locate the new scenario 501 to S20 After prompt and having typed the name of the scenario press ENTER A prompt will then ask for an INITIAL condition which will be the basis for the scenario Type in the appropriate initial condition 101 to 160 and press enter If accepted prompt line will add initial condition name and colour changes Page 5 4 5 2 1 3 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Initial Condition Directory An Initial Condition is a specific condition of the total simulation plant comprising a complete set of data and variables When activating the Init Condition push button a list of all created initial conditions appears To store an initial condition to later use the following procedure must
131. O 0603 A 16 03 00 Berth Time Some terminals limit berth time In order to fully outturn cargo it may be necessary to reduce ballasting time by taking on reduced ballast alongside and ballasting in river passage or ballasting during discharge Ballasting during discharge can take place only when the tanks to be ballasted have been fully stripped of cargo and the vessel has an efficient two valve separation There must be at least a two valve separation on the main pump room suction line between cargo and sea valves High Back Pressure Ballasting during discharge will increase the pumping time and will also make stripping difficult The discharge is to be sequenced so that minimum quantities remain in slop tanks for stripping During stripping the pumps may be lined up in sequence Stress Vessel must not exceed maximum calm water stress limits harbour condition at any time during cargo operations Page 5 56 Doc no SO 0603 A 16 03 00 The vessel may also have operating constraints such as Leaking pipelines Faulty valves Inoperative pumps Dirty sea chests Faulty inertgas plant These difficulties may be overcome during the discharge operation by a careful planned operation which compensates for them 5 5 4 Discharge Plans These plans are to be prepared prior to vessel s arrival and should include instructions on CHT2000 VLCC II ws User s Manual Discharge pumps and line to be used and discharging sequence and
132. ON STBD CROSSOVER PRESSURE G H X03354 CO SUCTION CROSSOVER OIL CONTENT I X03355 SW SUCTION PORT CROSSOVER OIL CONTENT J X03356 TC COW CROSSOVER OIL CONTENT K X03357 SLOP CROSSOVER OIL CONTENT L 03359 SW SUCTION STBD CROSSOVER OIL CONTENT V03365 0 1 SWSC SEA CHEST VALVE port V03369 0 1 SWSC SEA CHEST VALVE port Q V03367 0 1 SW SUCTION SEPARATION VALVE V03368 0 1 SWSC SEA CHEST VALVE stbd S V03364 0 1 SWSC SEA CHEST VALVE stbd T 2 48 Page 0061 M STRIPPING PUMP A B N03300 spm STRIPPING PUMP SPEED COMMAND N03301 spm STRIPPING PUMP SPEED 603304 m3 h STRIPPING PUMP FLOW E F P03310 bar STRIPPING PUMP DISCHARGE PRESS P03350 bar CO SUCTION CROSSOVER PRESSURE H I V03324 lt 0 1 gt STRIPPING PUMP SUCTION VALVE J V03325 lt 0 1 gt STRIPPING PUMP DISCHARGE VALVE K L 003303 m3 h STRIPPING PUMP STEAM FLOW M V03302 96 STRIPPING PUMP STEAM CONTROL VALVE 03326 lt 0 1 gt STRIPPING PUMP STEAM SUPPLY VALVE O P 03323 lt 0 1 gt SLOP CROSSOVER VALVE 603306 m3 h FLOW TO SLOP CROSSOVER S E Page 26 CHT2000 VLCC II ws Variable List 2 49 003340 003341 003345 03342 V03343 03346 P03352 P03350 SUAS OR OM a pp 03344 X03356 X03354 V03322 003305 HANAHVOZ 2 50 03610 203605 03611 03612 V03375 V03374 P03353 G03372 G03371 G03370 X03473 Z r m Q
133. P TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 14514 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC Page 61 N um 101353 V01356 001357 1360 1354 E01355 HP Z Q 2 9 Z Z ATT m Q m I 9 Q Z gt N N 201372 01326 01327 01330 01331 ASS m Q m m Ow gt P01345 P01346 P01347 Z01368 Z01369 ARANDVOZ Page 62 Doc no SO 0604 A January 6 1997 Page 0324 M CARGO TANK WT 4 P HEATING degC m3 h kW kW kW L 40 0 H 100 0 WT4P CARGO TEMPERATURE WT4P CARGO HEATING STEAM VALVE WT4P CARGO HEATING STEAM FLOW WT4P WT4P WT4P HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS 0325 CARGO TANK WT 4 P MISCELLANEOUS lt 0 2 gt bar L 0 1 L 0 0 H 0 1 H 8 0 kg M01332 kg bar bar bar DEG DEG WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 2 2 4 2 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING
134. P CLEAN OIL INTERFACE LEVEL WT6P CLEAN WTR INTERFACE LEVEL WT6P OIL CONTENT IN WTR OIL MIXTURE WT6P TOTAL TANK MASS incl residues WT6P TANK VOLUME 4024 m3 WT6P CLEAN OIL MASS WT6P DIRTY OIL MASS WT6P DIRTY WATER MASS WT6P CLEAN WATER MASS WT6P HARD RESIDUES WT6P SOFT RESIDUES WT6P DRIP RESIDUES WTOP OIL DENSITY at 15 dgrC WTO6P WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List N gt T02053 V02056 G02057 E02060 E02054 E02055 HYP Z Q 2 9 Z Z r ATT m Q m m 9 Q gt N 202072 2026 X02027 X02030 M02031 ASCH m Q a a 2 OQ m gt P02045 02046 2047 202068 702069 dJomNOVWOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0444 M CARGO TANK WT 6 P HEATING degC m3 h kW kW kW L 40 0 H 100 0 WT6P CARGO TEMPERATURE WT6P CARGO HEATING STEAM VALVE WT6P WT6P CARGO HEATING STEAM FLOW HEAT FROM STEAM WTOP HEAT LOSS TO SEA AIR WT6P HEAT LOSS TO ADJACENT TANKS Page 0445 M CARGO TANK WT 6 P MISCELLANEOUS 0 2 L 0 1 L 0 0 H 0 1 H 8 0 kg M02032 kg bar bar bar DEG DEG WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P WT6P IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 02 02 32 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TO
135. PARATOR OIL CONTENT G H I X03354 CO SUCTION CROSSOVER CONTENT J X03355 SW SUCTION PORT CROSSOVER OIL CONTENT 03356 TC COW CROSSOVER OIL CONTENT L X03357 SLOP CROSSOVER OIL CONTENT 03359 97 SW SUCTION STBD CROSSOVER CONTENT N O P X03312 SMALL DIAM LINE OIL CONTENT Q R M04164 tonn TOTAL TANK RESIDUE S T CHT2000 VLCC II ws Variable List Page 83 N N 75 P06000 06001 P06002 P06003 P06004 P06005 P06006 P06007 P06010 P06011 P06012 P06013 P06014 gt N E e Q06020 Q06021 Q06022 Q06023 Q06024 Q06025 H Q06026 I 006027 J Q06030 K Q06031 1 06032 M 006033 N Q06034 m gO Q m Page 84 Doc no SO 0604 A January 6 1997 Page 0600 M HULL SHEAR FORCES ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn ktonn L 20 0 L 16 0 L 18 0 L 20 0 L 18 0 L 16 0 L 16 0 L 18 0 L 22 0 L 18 0 L 14 0 L 12 0 L 20 0 H 20 0 H 16 0 H 18 0 H 20 0 H 18 0 H 16 0 H 16 0 H 18 0 H 22 0 H 18 0 H 14 0 H 12 0 H 20 0 SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE section 0 section 1 section 2 section 3 section 4 section 5 section 6 section 7 section 8 sect
136. PLACEMENT TOTAL CARGO MASS TOTAL HFO MASS TOTAL DO MASS TOTAL FW MASS Page 0700 M LOAD MASTER CONTROL lt 0 3 gt lt 0 1 gt kg m3 degC m lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt kg m3 lt 0 1 gt lt 0 1 gt degC lt 0 1 gt lt 0 1 gt L 0 0 H 0 0 INIT LOAD MASTER 1 2 3 EMPTY REAL LOADED TRANSFER LOAD MASTER DATA TO SIMULATOR SEA WATER DENSITY Load Master SEA WATER TEMP Load Master COMMON ULLAGE SETTING Load Master SET ULLAGE FOR ALL CARGO TANKS SET ULLAGE FOR ALL BALLAST TANKS COMMON VOLUME SETTING Load Master SET VOLUME FOR ALL CARGO TANKS SET VOLUME FOR ALL BALLAST TANKS COMMON DENSITY SETTING Load Master SET DENSITY FOR ALL CARGO TANKS SET DENSITY FOR ALL BALLAST TANKS COMMON TEMPERATURE SETTING Load Master SET TEMPERATURE FOR ALL CARGO TANKS SET TEMPERATURE FOR ALL BALLAST TANKS CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 169 Page 0701 M LOAD MASTER VOLUMES inputs A 06730 FPT TANK VOLUME Load Master B V06731 CT1 TANK VOLUME Load Master 06732 96 WT1S TANK VOLUME Load Master D V06733 WTIP TANK VOLUME Load Master E V06734 90 CT2 TANK VOLUME Load Master F V06735 96 WT2S TANK VOLUME Load Master G V06736 WT2P TANK VOLUME Load Master H V06737 96 WT3BS TANK VOLUME Load Master I V06740 90 WT3BP TANK VOLUME Load Master J V06741 CT3 TANK VOLUME Load Master 06742 96
137. RAIN VALVE DECK LINE 4 SHUT OFF VALVE lt 0 1 gt LOAD LINE 4 SHUT OFF VALVE lt 0 1 gt TC COW CROSSOVER VALVE lt 0 1 gt SLOP CROSSOVER VALVE lt 0 1 gt CO SUCTION CROSSOVER VALVE lt 0 1 gt SW SUCTION CROSSOVER VALVE lt 0 1 gt BOTTOM LINE 4 SHUT OFF VALVE CHT2000 VLCC II ws Variable List 2 33 V02712 2713 002714 2715 2716 2722 02710 02701 E02720 702721 702707 T m Q Z gt V02703 Q02706 G02704 Z02705 2 2 34 P03041 T03042 g Q gt tri V02711 R03040 R03046 X03047 2733 02734 02700 03066 ARAOVOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0041 M CARGO LINE 4 PUMP TURBINE m3 h bar bar bar L 0 0 rpm L 0 0 rpm kW 9 L 0 0 m3 h kWh kg H 20 0 COP4 DISCHARGE VALVE POS COP4 DISCHARGE VALVE POS COMMAND COP4 FLOW COP4 DISCHARGE PRESS before choke COP4 DISCHARGE PRESS after choke COP4 SUCTION PRESSURE H 1950 0 COP4 SPEED H 40 0 COP4 SPEED COMMAND COP4 POWER COP4 HYDRAULIC EFFICIENCY COP4 CAVITATION INDEX COP4 TURBINE STEAM CONTROL VALVE POS COP4 TURBINE SHAFT TORQUE TURBINE STEAM FLOW COP4 COP4 TURBINE EFFICIENCY Page 0042 M CARGO LINE 4 PUMP BEARING CONTROL bar L 1 0 degC L 0 0 lt 0 1 gt lt 0 1 gt lt 0 5 gt L 0 0 lt 0 1 gt lt 0 1 gt 5
138. RESSURE DROP CONSTANT R 5 03706 degC LOAD TEMPERATURE T 003707 kg m3 LOAD OIL DENSITY 2 4 0005 M MANIFOLD VALVES AND FLOWS V12162 lt 0 1 gt MANIFOLD 1 SHUT OFF VALVE 804 12362 0 1 MANIFOLD 2 SHUT OFF VALVE D 12562 0 1 MANIFOLD 3 SHUT OFF VALVE 804 12762 lt 0 1 gt MANIFOLD 4 SHUT OFF VALVE F 12163 0 1 MANIFOLD 1 SHUT OFF VALVE port H V12363 lt 0 1 gt MANIFOLD 2 SHUT OFF VALVE port I 12563 0 1 MANIFOLD 3 SHUT OFF VALVE port J V12763 lt 0 1 gt MANIFOLD 4 SHUT OFF VALVE port K 1 V02166 0 1 MANIF 1 2 CROSSOVER VALVE V02566 lt 0 1 gt 3 4 CROSSOVER VALVE N O G02141 m3 h LOAD FLOW to bottom line 1 Q G02341 m3 h LOAD FLOW to bottom line 2 R G02541 m3 h LOAD FLOW to bottom line 3 S 902741 m3 h LOAD FLOW to bottom line 4 Tp Page 4 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 5 0006 M MANIFOLD MONITOR X03627 lt 0 1 gt MANIFOLD MONITOR ACTIVE D X03625 lt 0 1 gt MANIFOLD MONITOR RESET COMMAND E F 003620 m3 h TOTAL MANIFOLD FLOW current H 603624 m3 h TOTAL MANIFOLD FLOW mean I J M03622 TOTAL MANIFOLD MASS K T03623 hour TOTAL MANIFOLD CONNECTION TIME L M N O P Q R S T 2 6 Page 0007 POLLUTION MONITOR A X03636 lt 0 1 gt POLLUTION MONITOR RESET COMMA
139. RGO TEMPERATURE WT4S CARGO HEATING STEAM VALVE WT4S WT4S CARGO HEATING STEAM FLOW HEAT FROM STEAM WT4S HEAT LOSS TO SEA AIR WT4S HEAT LOSS TO ADJACENT TANKS Page 0315 M CARGO TANK WT 4 S MISCELLANEOUS lt 0 2 gt bar L 0 1 L 0 0 H 0 1 H 8 0 kg M01232 kg bar bar bar DEG DEG WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WT4S WTAS WT4S IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 2 2 4 2 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT Page 59 N um og U01312 L01311 U01310 V01302 V01301 01303 01305 G01350 lt t m Q 3 m G01367 P01326 X01327 X01330 T01353 HaAROVOZ N N V01336 V01337 V01364 m QO m V01361 L V01362 M V01363 DO EO Pee Page 60 Doc no SO 0604 A January 6 1997 Page 0320 M CARGO TANK WT 4 P MAIN VARIABLES m m3 h m3 h bar degC 0 5 250 WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P L 0 1 0 1 WT4P 1 0 0 H 8 0 WT4P WT4P L 40 0 H 100 0 WT4P TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 14514 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TO
140. RIC PRESSURE F G P00426 bar L 0 1 0 1 CT2 TANK ATMOSPHERIC PRESSURE H P00526 bar 0 11 H 0 1 WT2S TANK ATMOSPHERIC PRESSURE I P00626 bar L 0 1 H 0 1 WT2P TANK ATMOSPHERIC PRESSURE J K P01126 bar L 0 1 H 0 1 CT3 TANK ATMOSPHERIC PRESSURE L P01226 bar 0 11 H 0 1 WT4S TANK ATMOSPHERIC PRESSURE 01326 bar 40 1 H 0 1 WT4P TANK ATMOSPHERIC PRESSURE N O P01426 bar L 0 1 H 0 1 CT4 TANK ATMOSPHERIC PRESSURE P P01526 bar 40 1 H 0 1 WTSS TANK ATMOSPHERIC PRESSURE P01626 L 0 1 0 1 WTSP TANK ATMOSPHERIC PRESSURE P01726 bar L 0 1 0 1 WT6S TANK ATMOSPHERIC PRESSURE S P02026 bar L 0 1 0 1 WT6P TANK ATMOSPHERIC PRESSURE T CHT2000 VLCC II ws Alarm List Page 5 Doc no SO 0604 A January 6 1997 2 5 70500 AG05 TANK CARGO TEMPERATURE 1 1 00153 degC 1 40 0 100 0 CARGO TEMPERATURE T00253 degC L 40 0 H 100 0 WTIS CARGO TEMPERATURE T00353 degC L 40 0 H 100 0 WTIP CARGO TEMPERATURE T00453 degC 1 40 0 H 100 0 CT2 CARGO TEMPERATURE 100553 degC L 40 0 H 100 0 WT2S CARGO TEMPERATURE T00653 degC L 40 0 H 100 0 WT2P CARGO TEMPERATURE 01153 degC 1 40 0 H 100 0 CT3 CARGO TEMPERATURE T01253 degC L 40 0 H 100 0 WT4S CARGO TEMPERATURE T01353 degC L 40 0 H 100 0 WT4P CARGO TEMPERATURE SUAS BODO 01453 degC 1 40 0 H 100 0 CT4 CARGO TEMPERATURE 101553 degC L 40 0 H 100 0 WTSS CARGO TEMPERATURE 01653 degC 40 00 H 100 0 WTSP CARGO TEMPERATURE 01753 degC L 40 0 H 100 0
141. RO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT CHT2000 VLCC II ws Variable List N 75 og U01612 L01611 U01610 V01602 V01601 01603 01605 001650 SUAS m Q 1 m G01667 P01626 X01627 X01630 T01653 N 25 V01636 V01637 Q m m 2 Q 2 gt H V01664 I V01668 J K V01661 L V01662 M V01663 32 OO Oo Doc no SO 0606 A January 6 1997 Page 0420 M CARGO TANK WT 5 P MAIN VARIABLES m m3 h m3 h bar degC L 0 5 250 WTSP WTSP WTSP WTS5P WTSP WTSP WTS5P WTSP WTSP 0 1 0 1 WTSP 1 0 0 H 8 0 WTS5P WTSP L 40 0 H 100 0 WTSP TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 8808 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE 0421 M CARGO TANK WT 5 P VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WTSP WTS5P WTSP WTS5P WTS5P WTSP WTS5P CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE STBD COW SUPPLY VALVE COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE
142. Re setting is achieved by clicking the RESET symbol after the pump has stopped The flashing light in the TRIP lamp will be extinguished if the cause for the trip has disappeared or turn to steady on light if the cause for the trip is still present This condition can be reset by the engineer i e the instructor Trip Causes The cause for the trip can be printed out on the instructor s printer and can also be identified on the display and on the instructor s VDU The trip causes are Overspeed Lub oil pressure low Bearing temperature high Discharge pressure high Inert Gas pressure are low low cargo pumps only The pump is stopped by clicking the symbol on the pump control section The turbine steam supply valve is closed and the pump is brought to stop after a while Page 5 41 5 4 5 4 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Loading Procedure Voyage Orders These instructions will be sent to the vessel by Charterers or Owners and will contain the following information Port s of loading and discharging Volume grade s and API Special requirements of the cargo ie heating Special properties of the cargo i e H5S Limitation of draft at discharge port Stemming details The vessel is responsible for loading under these orders The maximum amount of cargo to be loaded is dependant on the load line limitation filling ratio requirements or any particu
143. S 75 CARGO TANK WT 6 P 75 CARGO TANK WT 6 P FLOWS 76 CARGO TANK WT 6 P LEVELS MASSES 76 CARGO TANK WT 6 P HEATING 77 CARGO TANK WT 6 P MISCELLANEOUS 77 TANK SURVEY SOUNDINGS 78 TANK SURVEY MASSES C 78 TANK SURVEY VOLUMES 79 TANK SURVEY RELATIVE VOLUMES 79 TANK SURVEY TEMPERATURES 80 TANK SURVEY RESIDUES 80 TANK SURVEY EL AGE 81 TANK SURVEY ULLAGES mes 81 TANK COW VALVES id etm bcr Hebe deter ees 82 P V BYPASS VALVES eae 82 PIPING OIL RESIDUES 7 83 PIPING OIL RESIDUES 2 83 HULL SHEAR FORCES 84 HULL BENDING MOMENTS Nt 84 HULL DEFLECTIONS T 85 HULLSTCABILILY denen 85 86 LOAD MASTER RN 86 LOAD MASTER VOLUMES 87 Page v 2 170 2 171 2 172 2 173 2 174 2 175 2 176 2 177 2 178 2 179 2 180 2 181 2 182 2 183 2 184 Page vi Page 0702 M Page 0703 M Page 0704 M Page 0705 M Page 0706 M Page 0707 M Page 0708 M Page 0710 M Page 0711 M
144. T G P etc meaning CHT2000 VLCC II ws User s Manual Page 4 6 Temperature Flow Pressure Rpm Force Ampere Voltage Frequency Electrical Power Valve Level Position Signal Concentration Viscosity Constant Density Heat Transfer Mass Pump Fan Status Doc no SO 0603 A 9 January 1997 4 2 1 2000 Instructor System CHT2000 VLCC II ws User s Manual Page 4 7 Doc no SO 0603 A 9 January 1997 The instructor system is equipped with TEC2000 keyboard The keyboard includes a normal QWERTY keyboard Instructor section Alarm section and Operator section For detailed information see TEC2000 Instructor Manual Trackerball On the TEC2000 is a trackerball with 3 buttons on top Trackerball moves cursor on the screen Function of left button is START pump compressor or OPEN valve Centre button to operate screen BUTTONS or to open display windows Right button is opposite of left namely STOP pump compressor or CLOSE valve Function buttons INSTRUCTOR KEY OPERATOR Chooses between operator instructor status One push on the desired button will change status When key is LOCKED changing of operator status is not possible Key locks when turned CLOCKWISE CHT2000 VLCC II ws User s Manual Page 4 8 Doc no SO 0603 A 9 January 1997 INSTRUCTOR OPERATOR INIT COND OPERATION DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME
145. T meter STABILITY meter Sea Densitu D 1025 0 1BBB 210 35 1000 180 29 Aft L 18 51 GM Corr 15 50 Sea temp 25 00 C X of 96 17 Mid STBD L 18 30 FS Red 10 22 summer mark Mid PORT L 18 30 05 Rad E 14 91 Fwd L 18 09 Trim 10 43 Heel 10 09 p STRRBORRD 100 WT6P WTSP WT3P WT2P WTIP WT6S WTSS WT4S 42135 WT2S WT1S 80 60 40 20 0 slop bal x full 098 26 092 92 197 92 04 02 098 79 VS6 64 V97 99 098 083 098 01 97 07 UB0 00 098 098 092 46 197 59 10 02 193 99 496 54 0826 66 0819 98 0826 66 1025 0 0819 99 0819 99 0819 99 0819 99 0819 99 0819 99 01625 6 0826 66 0819 98 0826 66 01625 6 0819 99 0819 99 put 68 00 151512 60 00 G6 06 68 08 68 00 60 00 69 08 9 08 9 98 68 00 698 08 68 00 60 00 0 Quantity M3185 5 M6576 6 M1141 1 0 M7354 6 M9674 7 M24207 M24239 M24223 M23983 M3177 2 M6537 3 M11364 M1 00 M7003 5 M9724 6 Port M 38 19 ktonnes Center 86 65 ktonnes Starboard M 37 81 ktonnes 281 To Bunkers and Water Bargraphs Total 172 55 ktonnes CHT2888 ULCC II REV 1 3 CHT2000 VLCC II ws User s Manual Page 5 26 5 3 3 4 5 3 3 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Tank levels Tanks levels are changed dynamically by changing the volumes of liquid in the tanks The volume of liquid in the tanks is changed by generating flows to or from the tanks Flows can be generated in two ways Gravity flow Pump f
146. T FLOW CNTR SUCTION BOTTOM OUTLET FLOW PORT SUCTION SLOP SEPARATOR SUCTION FLOW BALANCE FLOW FROM PORT TO STBD SLOPT WT6S WT6S WT6S WT6S WT6S WT6S TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW DECK TOTAL SUCTION BOBBLE FLOW 0433 M CARGO TANK WT 6 S LEVELS MASSES m m m m WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 4024 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC Page 73 N A 95 01753 V01756 001757 1760 1754 1755 N Z01772 P01726 X01727 X01730 m Q m m OO Z gt P01745 P01746 P01747 Z01768 Z01769 Page 74 Doc no SO 0604 A January 6 1997 Page 0434 M CARGO TANK WT 6 S HEATING degC m3 h kW kW kW L 40 0 H 100 0 WT6S CARGO TEMPERATURE WT6S CARGO HEATING STEAM VALVE WT6S WT6S WT6S WT6S CARGO HEATING STEAM FLOW HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS Page 0435
147. T6S WT5S WT4S WwT3S WT2S WTIS 80 60 4 20 9 slop bal bal slop bal full 998 26 092 92 Y97 92 00 02 098 76 096 04 997 99 098 08 098 01 87 07 00 08 098 08 092 46 197 58 00 02 193 98 096 54 pec 0828 08 0819 98 0820 00 D1025 0 0819 99 0819 99 0819 99 0819 99 0819 99 0819 99 01025 0 0820 00 0818 98 0820 00 01925 80 0819 99 0819 99 Flon out 50 00 60 08 60 08 60 00 60 00 60 00 60 00 60 00 60 00 60 00 60 00 60 00 60 00 88 08 80 00 60 00 GO 00 Quantity M3185 5 M6570 0 11401 1 04 M7354 0 M9674 7 M24207 M24239 M24223 M23983 0 00 3177 2 6537 3 M11364 1 08 7003 5 9 24 6 Port 38 19 ktonnes Center 96 65 ktonnes Starboard 37 81 201 To Bunkers and Water Bargraphs Total 172 65 ktonnes CHT2066 VLCC II REV 1 3 Cargo Baragraph will give the operator a total view of the cargo and ballast tanks with information about tank level flow rate cargo density and quantity in each tank CHT2000 VLCC II ws User s Manual Page 4 43 Doc no SO 0603 A 9 January 1997 4 5 2 Cargo Survey Alarm Group Cargo Survey 00 00 32 Picture Running 102 Ullage meter L PORT bal 025 28 MEN 10 5 slop ua s2 A 11 85 A Ullage meter CENTER 51 A A Y 026 00 I uo CT 2 CT 1 122 201 19 HFO 124 201 ST
148. TAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE 0321 M CARGO TANK WT 4 P VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT4P WT4P WT4P WT4P WT4P WT4P BOTTOM VALVE CNTR BOTTOM VALVE STBD COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List N um 1 gt G01341 G01342 G01317 G01343 G01344 001333 001334 lt 001370 2 118 001310 101311 101313 L01314 X01316 M01303 V01302 M01322 M01323 M01324 M01325 M01307 M01306 M01315 D01320 D01321 Q Z O 2 O Z i R r Q m i 9 Q Z gt CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0322 M CARGO TANK WT 4 P FLOWS m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT4P WT4P WT4P WT4P WT4P WT4P WT4P BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW Page 0323 M CARGO TANK WT 4 P LEVELS MASSES m m m m WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4P WT4
149. TAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT Page 77 Doc no SO 0604 A January 6 1997 2 151 Page 0500 M TANK SURVEY SOUNDINGS L00011 m FPT SOUNDING even keel B L00111 m CT1 SOUNDING even keel 100211 WT1S SOUNDING even keel D L00311 m WTIP SOUNDING even keel E L00411 m CT2 SOUNDING even keel F L00511 m WT2S SOUNDING even keel G L00611 m WT2P SOUNDING even keel H L00711 m WT3BS SOUNDING even keel I L01011 m WT3BP SOUNDING even keel J L01111 m CT3 SOUNDING even keel K L01211 m WT4S SOUNDING even keel L L01311 m WT4P SOUNDING even keel M L01411 m CT4 SOUNDING even keel N L01511 m WTSS SOUNDING even keel L01611 m WTSP SOUNDING even keel P L01711 m WT6S SOUNDING even keel L02011 m WT6P SOUNDING even keel R S L04112 FORE HFO TANK SOUNDING T L04122 m AFT HFO TANK SOUNDING 2 152 Page 0501 M TANK SURVEY MASSES A M00003 tonn FPT TOTAL TANK MASS incl residues B M00103 tonn CT1 TOTAL TANK MASS incl residues M00203 tonn WT1S TOTAL TANK MASS incl residues D M00303 tonn WTIP TOTAL TANK MASS incl residues E M00403 tonn CT2 TOTAL TANK MASS incl residues F M00503 tonn WT2S TOTAL TANK MASS incl residues G M00603 tonn WT2P TOTAL TANK MASS incl residues H M00704 tonn WT3BS TOTAL TANK MASS incl residues I M01004 tonn WT3BP TOTAL TANK MASS incl residues J M01103 tonn CT3 TOTAL TANK MASS
150. TANK WT 6 S MAIN VARIABLES m m3 h m3 h bar degC L 0 5 250 WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S WT6S L 0 1 0 1 WT6S L 0 0 8 0 WT6S WT6S L 40 0 H 100 0 WT6S TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 4024 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0431 M CARGO TANK WT 6 S VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT6S WT6S WT6S WT6S WT6S WT6S BOTTOM VALVE CNTR BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List N gt E G01741 G01740 G03470 G03450 001717 m Q m a Q gt G01743 G01744 S 001733 001734 001770 2 142 001710 101711 101713 101714 1716 01703 01702 M01722 M01723 M01724 M01725 M01707 M01706 M01715 D01720 D01721 Q Z O 2 O Z lt i R Q Z gt CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0432 M CARGO TANK WT 6 S FLOWS m3 h m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT6S WT6S BOTTOM OUTLE
151. TION VALVE CHT2000 VLCC II ws Variable List ve V02112 V02113 G02114 P02115 2116 2122 02110 N02101 E02120 702121 702107 SUAS n Q m m 9 Q 2 gt V02103 Q02106 G02104 Z02105 2 10 2241 T02242 g Q gt tri V02111 R02240 R02246 X02247 m Q m R02133 R02134 02100 02266 3JONOVUOZ CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0011 M CARGO LINE 1 PUMP TURBINE m3 h bar bar bar L 0 0 rpm L 0 0 rpm kW L 0 0 m3 h kWh kg H 20 0 COP1 DISCHARGE VALVE POS COP1 DISCHARGE VALVE POS COMMAND COP1 FLOW COP1 DISCHARGE PRESS before choke COP1 DISCHARGE PRESS after choke COP1 SUCTION PRESSURE H 1950 0 COP1 SPEED H 40 0 COP1 SPEED COMMAND COP1 POWER COP1 HYDRAULIC EFFICIENCY CAVITATION INDEX COP1 TURBINE STEAM CONTROL VALVE POS COP1 TURBINE SHAFT TORQUE TURBINE STEAM FLOW COPI TURBINE EFFICIENCY Page 0012 M CARGO LINE 1 PUMP BEARING CONTROL bar L 1 0 degC L 0 0 lt 0 1 gt lt 0 1 gt lt 0 5 gt L 0 0 lt 0 1 gt lt 0 1 gt 5 0 H 60 0 H 1 0 COP1 BEARING LO PRESSURE COP1 BEARING TEMPERATURE COP1 RECIRCULATION VALVE POS LUB OIL PUMP START COP1 START STOP TRIP INDICATION COP1 SPEED SURGE CONTROL AUTO SWITCH COP1 FLOW SURGE CONTROL AUTO SWITCH
152. Valves and Pumps The cargo ballast valves are operated mainly from the cargo line and pump mimics CHT2000 VLCC II ws User s Manual Page 5 29 5 3 3 8 5 3 3 9 5 3 3 10 5 3 3 11 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Pump Tank and Valve overview The cargo ballast valve configuration is shown in the Load Discharge Ballast routing picture MD 206 and deck bottom line pictures This picture is not dynamic Bottom Valves The bottom valves are on off valves and throttle valves They are operated from the cargo bottom lines picture MD 110 On off Valves The on off bottom valves are used during normal loading discharging The valves are operated by means of the OPEN and CLOSE clicking on the valve symbol Throttle Valves The throttle bottom valves can be used to achieve a more accurate control of the flow during the last stage of loading topping up These valves are positioned closer to the bulkheads and closer to the bottom than the on off valves The throttling bottom valves are operated by the SELECT clicking on the symbol The current valve position can be read on indicating meter and changed by entering a new value between 0 100 followed by ENTER Page 5 30 Doc no SO 0603 A 16 03 00 5 3 3 12 Cross over Valves The cross over valves in the pump room are modelled as on off valves and are operated by an OPEN and CLOSE clicking on the symbol CHT2000 VLCC II ws User s Manual Pa
153. W kW kW L 40 0 H 100 0 WT2S CARGO TEMPERATURE WT2S CARGO HEATING STEAM VALVE WT2S WT2S WT2S WT2S CARGO HEATING STEAM FLOW HEAT FROM STEAM HEAT LOSS TO SEA AIR HEAT LOSS TO ADJACENT TANKS Page 0215 M CARGO TANK WT 2 S MISCELLANEOUS 0 2 bar L 0 1 L 0 0 H 0 1 H 8 0 kg M00532 bar bar bar DEG DEG WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S WT2S IG INITIATION 1zair 2 IG TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT INERT GAS MASS 02 02 32 HYDRO CARBON MASS LIQUID GAS PRESSURE GEODETIC PRESSURE TOTAL TANK BOTTOM PRESSURE TANK CLEANING UPPER LIMIT TANK CLEANING LOWER LIMIT CHT2000 VLCC II ws Variable List 2 93 og 000612 L00611 U00610 00602 V00601 00603 00605 000650 lt t 1 Q 1 m G00667 P00626 X00627 X00630 T00653 ARAN VOZ 2 94 0636 00637 gt 00664 00668 J 00661 L V00662 M V00663 Doc no SO 0606 A January 6 1997 Page 0220 M CARGO TANK WT 2 P MAIN VARIABLES m m3 h m3 h bar degC 0 5 250 WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P WT2P L 0 1 0 1 WT2P 1 0 0 H 8 0 WT2P WT2P L 40 0 H 100 0 WT2P TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 9283 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl resi
154. WT3P TANK ULLAGE measured WT3BP SOUNDING even keel WT3P TANK ULLAGE even keel WT3BP TANK VOLUME cap 5231 m3 WT3BP CLEAN WATER MASS WT3BP BOTTOM VALVE WT3BP BOTTOM OUTLET FLOW WT3BP TANK TOP OVERFLOW Page 0241 M BALLAST TANK WT 3 P MISCELLANEOUS degC L 40 0 H 100 0 WT3BP TEMPERATURE kW kW bar bar bar kg m3 WT3BP HEAT LOSS TO SEA AIR WT3BP HEAT LOSS TO ADJACENT TANKS WT3BP LIQUID GAS PRESSURE WT3BP GEODETIC PRESSURE WT3BP TOTAL TANK BOTTOM PRESSURE WT3BP WTR DENSITY at 15 dgrC Page 53 N 97 og U01112 L01111 U01110 V01102 V01101 M01103 M01105 G01150 SUAS homes G01167 P01126 X01127 X01130 01153 2 N E e V01136 V01137 V01135 m Q m m g Q gt V01164 m lt CN L V01162 M V01163 Page 54 Doc no SO 0604 A January 6 1997 0300 M CARGO TANK CT 3 MAIN VARIABLES m m3 h m3 h bar degC 105 250 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 0 1 H 0 1 CT3 L 0 0 8 0 CT3 CT3 L 40 0 H 100 0 CT3 TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 30818 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Pag
155. WT4S TANK VOLUME Load Master L 06743 WT4P TANK VOLUME Load Master V06744 CT4 TANK VOLUME Load Master N 06745 96 WTSS TANK VOLUME Load Master V06746 WTSP TANK VOLUME Load Master 06747 WT6S TANK VOLUME Load Master 06750 WT6P TANK VOLUME Load Master R V06751 FHFO TANK VOLUME Load Master S V06752 96 AHFO TANK VOLUME Load Master T 2 170 Page 0702 LOAD MASTER DENSITIES inputs A D06700 kg m3 FPT LIQUID DENSITY Load Master 206701 kg m3 CT1 LIQUID DENSITY Load Master 006702 kg m3 WT1S LIQUID DENSITY Load Master D 006703 kg m3 WTIP LIQUID DENSITY Load Master 206704 kg m3 CT2 LIQUID DENSITY Load Master 206705 kg m3 WT2S LIQUID DENSITY Load Master G 206706 kg m3 WT2P LIQUID DENSITY Load Master H 206707 kg m3 WT3BS LIQUID DENSITY Load Master D06710 kg m3 WT3BP LIQUID DENSITY Load Master J D06711 kg m3 CT3 LIQUID DENSITY Load Master K D06712 kg m3 WT4S LIQUID DENSITY Load Master L D06713 kg m3 WT4P LIQUID DENSITY Load Master M D06714 kg m3 CT4 LIQUID DENSITY Load Master N D06715 kg m3 WTSS LIQUID DENSITY Load Master O D06716 kg m3 WTSP LIQUID DENSITY Load Master P D06717 kg m3 WT6S LIQUID DENSITY Load Master Q D06720 kg m3 WT6P LIQUID DENSITY Load Master R 5 CHT2000 VLCC II ws Variable List Page 87 Doc no SO 0604 A January 6 1997 2 171 Page 0703 M LOAD MASTER TEMPERATURES inputs A T06
156. Z EF Page 34 Doc no SO 0604 A January 6 1997 0100 M CARGO TANK CT 1 MAIN VARIABLES m m3 h m3 h bar degC 0 5 H 25 0 CTI 0 1 H 0 1 L 0 0 H 8 0 L 40 0 H 100 0 CTI TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 30813 m3 TOTAL TANK LIQUID VOLUME TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0101 M CARGO TANK CT 1 VALVES 0 1 96 0 1 0 1 0 1 0 1 BOTTOM VALVE CNTR BOTTOM VALVE STBD BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List 2 65 9000141 600142 000140 000117 000143 000144 Pon z gt Q r i J r m gt G00133 G00134 lt G00170 2 66 000110 L00111 L00113 L00114 X00116 M00103 V00102 M00122 M00123 M00124 M00125 M00107 M00106 M00115 D00120 D00121 2 Z Q 9 O Z lt 2 AST r Q m m 9 Q Z CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0102 M CARGO TANK CT 1 FLOWS m3 h m
157. age 4 52 Doc no SO 0603 A 9 January 1997 4 5 10 Cargo Bottom Lines 00 23 14 Picture Alarm Running HD Cargo Bottom Lines NN 1 peed NECI NECI I 5 21 1 Fe Hire 1 L e Hee He Hie 1 TH i Ebo 2 2 22222222 2224 4 E ES 0 i i 1 Wo faa ta t 1 1 1 pa Es 1 454 454 1 1 1 Bot line 1 1 1 FPT me Bot line 3 1 j Ballast line 1 1 Bot line 2 pu I T Hee Bot line 1 RO aay Fd M 8 8 I i 1 h 1 6 92 eee PERI 3 1 TEE a Feee Las i Lage Hege Dues 2 4 4 0 0 4 6 lt 0 0 i lt 0 0 4 0 0 1 LI I I 1 1 1 1 1 5 1 CHT2000 ULCC II REV 1 2 Cargo Bottom Lines MD 110 contains an overall view of line arrangement in cargo and ballas
158. alve V0135 closed C M0103 0 100 CT 1 bottom valve V0137 leakage D 0104 0 1 bottom valve 0137 closed E M0105 0 1 CT bottom valve V0136 leakage F M0106 0 1 bottom valve V0136 stuck M0111 0 100 CT 2 bottom valve V0435 leakage H 0112 0 1 2 bottom valve V0435 closed I M0113 0 100 CT 2 bottom valve V0437 leakage J 0114 0 1 2 bottom valve V0437 closed M0115 0 1 2 bottom valve V0436 leakage L M0116 0 1 2 bottom valve V0436 stuck M N O P Q R 5 2 1 Page 0200 MA02 CENTRE TANK 3 4 VALVES A M0201 0 100 3 bottom valve V1135 leakage M0202 0 1 CT 3 bottom valve V1135 closed M0203 0 100 3 bottom valve V1137 leakage D M0204 0 1 3 bottom valve V1137 closed E M0205 0 1 CT 3 bottom valve V1136 leakage M0206 0 1 CT 3 bottom valve V1136 stuck M0211 0 100 CT 4 bottom valve V1435 leakage H M0212 0 1 4 bottom valve V1435 closed I M0213 0 100 CT 4 bottom valve V1437 leakage J M0214 0 1 4 bottom valve V1437 closed M0215 0 1 CT 4 bottom valve V1436 leakage L M0216 0 1 4 bottom valve V1436 stuck M N O P Q R S T CHT2000 VLCC II ws Malfunction List Page 3 Doc no SO 0604 A January 6 1997 2 2 Page 0300 MA03 BALLAST TANK VALVES A M0301 0 100 bottom valve V0035 leakage M0302 0 1 bottom valve V0035 closed C M0303 0 100 WT3BS bottom valve V07
159. any special operational procedures Ballasting after discharge Method of how to stop cargo pumps and to raise alarm in case of fire or pollution Copy of the discharge plan should be given to Terminal representative Page 5 57 5 5 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Cargo Loss Control During discharge the following measures are to be taken All cargo tanks are to be stripped using the most effective method Every effort is to be made to pump ashore the maximum amount of cargo Final stripping of all tanks is to be carried out when all main cargo tanks have been discharged The cargo tanks are to be systematically drained from forward to aft into the port slop tank After this process the slop tank is to be discharged by main cargo pump to the lowest possible level in the tank The remaining cargo is to be stripped ashore Main cargo lines are to be drained into the slop tank before final stripping is performed Final stripping to be carried out by using the piston stripping pump and discharged ashore through the Small Diameter Line Page 5 58 5 5 6 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Instructions during and after Discharge It is of major importance that maximum diligence is used by the vessel student during the final discharging to avoid damage or pollution claims Make sure that vessel is trimmed to maximum allowable trim stern during t
160. any time The effect of temperature variation night day on the tank pressure and the effect of the tank s constant pressure vacuum is modelled A P V valve is provided on each tank The inert gas plant is fitted with two air inlets one for each fan allowing the plant to take air instead of flue gas for ventilating and gas freeing cargo tanks CHT2000 VLCC II ws User s Manual Page 4 66 Doc no SO 0603 A 9 January 1997 4 5 26 Cargo Oil Pump 1 2 3 amp 4 and Separator EA aai Crude Oil Pump 1 Separator rs NER isa TURBI FE Effici VACEUH SEP To Sloe eu 2218 50 ra Shaft 025 31 Level pce 012 cores Inlet liquid 99838 3 n n Dutlat Liquid 6429 3 Win 10141 19 08 2 p ma WR us Pt S E sn ME 3 29 L 4 00 81 be go Fue Eras Tripped FEET CHTNNW ULCE II REUS 1 2 PRINT REPORT UNIT CONVERSION The cargo pumps are modelled as steam driven centrifugal pumps The pump model is of a general type and can represent any type of centrifugal pumps Each cargo pump is equipped with an oil gas separator for stabilising the pump suction head and reduce cavitation during the last phase of emptying the tank stripping operation For the cargo pumps special attention is paid to the simulation of possible cavitation during stripping opera
161. are programmed by means of selecting the upper and lower limit in degrees by setting the required value in the control windows MD 220 Page 5 103 Doc no SO 0603 A 6 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Appendix A Trip Codes CHT2000 VLCC II ws User s Manual H Doc no SO 0603 A 6 January 1997 1 APPENDIX A TRIP CODES H This appendix shows the trip code and the failure malfunction causing trip of the following machinery 1 1 X2247 CARGO PUMP 1 1 Overspeed 2 LO Press LL 3 Bearing Temp HH 4 Pump Discharge Pressure HH 5 Low Inertgas Pressure Main Line 1 2 X2447 CARGO PUMP 2 1 Overspeed 2 LO Press LL 3 Bearing Temp HH 4 Pump Discharge Pressure HH 5 Low Inertgas Pressure Main Line 1 3 X2647 CARGO PUMP 3 1 Overspeed 2 LO Press LL 3 Bearing Temp HH 4 Pump Discharge Pressure HH 2 Low Inertgas Pressure Main Line CHT2000 VLCC II ws User s Manual 122 2169 rpm 0 40 bar 80 Deg C 250 mWC 0 4 mWC 122 2169 rpm 0 40 bar 80 Deg C 250 mWC 0 4 mWC 122 2169 rpm 0 40 bar 80 Deg C 250 mWC 0 4 mWC Page 1 1 Doc no SO 0603 A 6 January 1997 1 4 X3047 CARGO PUMP 4 1 Overspeed 2 LO Press LL 3 Bearing Temp HH 4 Pump Discharge Pressure HH 5 Low Inertgas Pressure Main Line 1 5 X32447 BALLAST PUMP 1 Overspeed 2 LO Press LL 3 Bearing Temp HH 4 Pump Discharge Pressure HH CHT2000 VLCC II ws User s Manual H
162. ations of student response during simulation Active in instructor mode only Input of specified measuring variables under tag name Specify upper and lower limits Will evaluate how process is kept by student during simulation Evaluation criteria is whether student is able to maintain process within specified limits Running Starts simulation after init conditions or freeze Active only in instructor mode When RUNNING button is pushed a prompt will inform that simulation is started Freeze Freezes simulation during breaks or when situation needs time out for evaluation Active only in instructor mode When FREEZE button is pushed a prompt will inform that simulation is halted CHT2000 VLCC II ws User s Manual Page 4 20 Doc no SO 0603 A 9 January 1997 INSTRUCTOR n 11 INIT COND OPERATION SCENARIO DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE Stop Ends simulation after a prompt Pressing STOP and typing yes after prompt will log out of simulator completely Active in both modes To restart Type LOGIN and press ENTER Type sim in both login name and password Remember to press ENTER after each input Select one of offered options Load initial condition by pressing selected condition button Initial condition found in INITIAL CONDITIONS DIRECTORY CHT2000 VLCC II ws User s Manual
163. bulkheads than the main bottom valves Low liquid level in a tank may cause influx of air into the pipelines if the main valve is kept open CHT2000 VLCC II ws User s Manual Page 4 74 Doc no SO 0603 A 9 January 1997 4 9 1 Tank Atmosphere 01 53 52 Picture Alarm E Running MD 222 Center Tank 1 Atmosphere Group 5 Center GAS FLOW W flammable mixture 122 Inert inlet 6 1462 0 m3 h 100 25 INERT GAS DECK LINE 0 e 1 59 AX 2 HC 5 51 z Pressure P0 03 Abar 6a 15 HC Z TANK ATMOSPHERE Chydro 0 4 1 68 AZ carbon HC X36 62 7 Pressure P0 03 Abar 10 MISC TANK DATA 5 Volume 87 19 Z full Dens oil 0 819 99 kg m Dens water D 1025 0 kg m L Disch Rate 6 2924 5 m h Liq Content M21547 tonnes 9 5 10 ate 2 oxygen Modelling of the Tank Atmosphere The vapour content in the tanks comprises inert gas and hydrocarbon gas The content of inert gas can be read absolutely mass of inert gas The content of oxygen can be read as a relative part of the inert gas The content of hydrocarbon gas can be read either absolutely mass of hydrocarbon gas or relatively hydrocarbon gas Oxygen Content The relative content of oxygen in a tank will be the result of the mixing between Actual content of oxygen in the tank Total mass of inert gas in the tank Oxygen content of the inert gas flow inserted into the tank Inert gas flow rate
164. ch other Storage must take place indoors CHT2000 VLCC II ws User s Manual Page 3 1 Doc no SO 0603 A 9 January 1997 3 3 Environmental Requirements Local climate conditions and the system configuration are essential to the requirements for heating ventilation and air conditioning The heating ventilation and air conditioning system must provide a sufficient air flow with correct temperature and humidity Ideal temperature 23 CF 3 C Ideal relative humidity 50 10 Dust The air pressure in the simulator rooms should be higher than the pressure outside Special demands are made on the air conditioning units filter if the air includes corrosive gases salts conductive particles or other unusual particles of dust Minimum and maximum requirements when in operation Minimum temperature lt 10 C Maximum temperature 30 C Relative humidity 10 to 95 condensation If the humidity is lower than 40 there may be problems with static electricity To ensure a reliable operation of the air conditioning unit preventive maintenance should be carried out regularly A thermo stat must be installed in the different rooms so the temperatures can be set individually NOTE The Air Conditioning equipment must include an automatic restart after a power failure There is a requirement to maintain air conditioning even if equipment is shut down because parts of the system remain energized If the humidity
165. d 5 2 Operating PANO IS 5 3 Function buttons at the Instructor 5 3 SEO 5 15 Function buttons at the Operator section 5 16 Cargo Handling Training from the Graphic Workstation 5 21 err 5 22 Picture Directory 2 LOAD MASTER 5 23 General Operatig Nt 5 25 TAG ee 5 42 boob CT 5 42 Planning Cargo Stowage 5 43 The Loading 5 45 BUE inr T S 5 47 Lining up Pipelines and Valves Ne 5 47 HQ 5 49 iuter D b ebd 5 49 Commencement of Loading 5 50 Monitoring Cargo Inr 5 51 Chane me ui T 5 51 CHT2000 VLCC II ws User s Manual Page iii 5 4 11 5 4 12 5 4 13 5 5 5 5 1 5 5 2 5 33 5 5 4 5 5 5 5 5 6 5 6 5 6 1 5 6 2 5 6 3 5 6 4 5 6 5 5 6 6 5 6 7 5 6 8 5 6 9 5 6 10 5 7 5 7 1 5 7 2 5 7 3 5 7 4 5 7 5 5 7 6 5 7 7 5 7 8 5 7 9 5 7 10 5 7 11 5 7 12 5 7 13 5 7 14 5 7 15 5 7 16 5 8 5 8 1 5 8 2 5 8 3 5 8 4 5 8 5 Doc no SO 0603 A 9 January 1997
166. d G4639 3 Mavh Outlet liquid 64639 5 Mavh Runpiicunves Inlet gas G8 00 m h Outlet gas 68 98 Anti AUTO __ Valve 4168 8 1 65 Surge Ctr i an P9 28 d pressure 1 A Level U 166 66 nti 270 urse WAN s Speed P 10 48 A N 1900 08 208 Steam Cargo Pump G4639 3 liquid 114 STOP 4 00 08 9 gas 3 Tripped i Prim 1 meter gt RESET Tri Vacuum Separator CHT2888 ULCC II REV 1 2 UNIT PRINT CONVERSION REPORT CHT2000 VLCC II ws User s Manual Page 5 38 5 3 3 15 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Oil Gas Separator with Vacuum Pump The cargo pumps are furnished with oil gas separators with vacuum pumps The vacuum pumps are started automatically at low liquid level in the separator The state of the vacuum pump is shown by a running light Pump symbol changes colour from black to Grey If the liquid level in the oil gas separator becomes too low gas or air will enter into the pump and cause cavitation lost pumping capability and pump overspeed These problems can occur if the vacuum pump does not start automatically at low level The result can be demonstrated by setting the vacuum pump in manual under low liquid level For training purposes the pump speed and the discharge valve opening can be controlled separately from each other However modern cargo control techniques for
167. d by illuminated actual P V Valve During loading discharging the gas pressure may change too much to be regulated by the P V Valve The P V by pass Valve Tank hatch may be opened P V by pass valves should not be opened during the discharging operation because it will increase of O2 in the cargo tanks atmosphere 5 9 Tank Cleaning Water and COW Permanently high capacity tank washing machines are installed in all tanks As a general rule all tank cleaning TC should take place in inerted atmosphere and the O5 concentration in the tank to be below 8 by volume CHT2000 VLCC II ws User s Manual Page 5 99 61 32 48 Running Picture MD 122 Center Tank 1 Condition Doc no SO 0603 A 16 03 00 Alarm Group LIQUID Temp T59 18 A C Full U88 36 ULLAGE meter Measured 02 84 A SOUNDING meter Total L22 67 Clean 011 18 02 Mix Water 0 00 Perc of oil MASS tonnes Total M22883 Clean M22057 Dirty Dirty Ma aa Clean RESIDUES tonnes M26 48 Total Hard M6 09 Soft M3 95 Drip 1 Center Tank 1 Atmosphere G1426 6 M 7h P 0 03 222 liquidf 60 00 A gas 100 08 h Out on deck 6892 74 P10 76 UU a P0 03 A 25 I 295404 20 i 15 5 heater ee liquid level m gt soft hard 60 00 E8 80 kW
168. d initial conditions Active in instructor mode only Instructor To create an initial condition play until desired running status is obtained This is done in the same fashion as running an actual plant Opening valves and starting pumps until a stable running condition on different levels is achieved When satisfied with simulator situation chose display INITIAL CONDITION and click on CREATE Type in name of condition and press enter When various levels of complexity have been recorded these initial conditions can be run under scenario to create realistic simulations of actual on board situations with the assistance of malfunction editor and scenarios To load an initial condition click with centre trackerball button on chosen condition Loading of initial condition in FREEZE mode only CHT2000 VLCC II ws User s Manual Page 4 11 Doc no SO 0603 A 9 January 1997 Operating Conditions Sets the response to actions during simulation Active in instructor mode only Instructor Picture is divided into 9 windows where parameter responses can be set Access Different access levels can be set Ordinarily only instructor can access OPERATION CONDITIONS to establish simulation parameters Fixed process Instructor can set some systems in permanent no alarms condition Useful when sub systems are to be simulated without disturbances Inhibit keyboard buzzer Toggles buzzer sound active inactive Levels Sets si
169. dues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE 0221 M CARGO TANK WT 2 P VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WT2P WT2P WT2P WT2P WT2P WT2P WT2P CHT2000 VLCC II ws Variable List BOTTOM VALVE CNTR BOTTOM VALVE STBD COW SUPPLY VALVE COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE Page 49 2 95 gt G00641 000642 903262 000617 000643 000644 600633 G00634 lt G00670 2 96 U00610 L00611 L00613 L00614 X00616 M00603 00602 00622 00623 00624 00625 00607 00606 M00615 200620 200621 2 O 9 O Z lt 2 AST r Q m m 9 Q Z Page 50 Doc no SO 0604 A January 6 1997 Page 0222 M CARGO TANK WT 2 P FLOWS m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 WT2P WT2P BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION BW DROP FLOW INTO TANK WT2P WT2P WT2P WT2P WT2P WT2P WT2P TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW 0223 M CARGO TANK 2 LEVELS MASSES m m m m WT2P
170. e 0301 M CARGO TANK CT 3 VALVES lt 0 1 gt 96 0 1 0 1 0 1 0 1 CT3 CT3 CT3 CT3 CT3 BOTTOM VALVE CNTR BOTTOM VALVE STBD BOTTOM VALVE PORT COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List N gt 001141 601142 601140 001117 001143 001144 on z gt Q r ri GO m gt G01133 G01134 lt G01170 2 106 001110 101111 101113 101114 X01116 01103 V01102 M01122 01123 01124 01125 M01107 M01106 M01115 D01120 D01121 Q Z O 2 O Z lt z R r Q m i 9 Q Z gt CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 0302 CARGO TANK CT 3 FLOWS m3 h m3 h m3 h m3 s m3 h m3 h m3 h m3 h L 0 0 H 1 0 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 BOTTOM OUTLET FLOW CNTR SUCTION BOTTOM OUTLET FLOW STBD SUCTION BOTTOM OUTLET FLOW PORT SUCTION TANK TOP OVERFLOW COW CLEANING FLOW SWW CLEANING FLOW INERT GAS FLOW FROM MAIN LINE INERT GAS FLOW TO DECK TOTAL SUCTION BOBBLE FLOW Page 0303 M CARGO TANK CT 3 LEVELS MASSES m m m m CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 CT3 TANK ULLAGE even keel SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL
171. ed LM FREE SURFACE reduction LM DYNAMIC STABILITY area 0 40 dgr LM CHT2000 VLCC II ws Variable List N 07053 507501 507502 507503 507504 507505 507506 507507 507508 507509 507510 507511 507512 507513 N E N X07110 X07111 Z03513 V03563 Q m Q gt X07053 3 2 Z Q 2 9 Z K T AS Doc no SO 0606 A January 6 1997 Page 0800 M MOTION PLATFORM CONTROL lt 0 1 gt ACTIVATE MOTION PLATFORM 1 lt 0 1 gt MP gt HYDRAULIC OIL LEVEL OK lt 0 1 gt MP gt HYDRAULIC OIL PRESS OK lt 0 1 gt MP gt HYDRAULIC OIL TEMP OK lt 0 1 gt MP gt MAIN DOOR CLOSED lt 0 1 gt MP gt EMERGENCY DOOR CLOSED lt 0 1 gt MP gt GANGWAY RETRACTED lt 0 1 gt MP gt POWER PACK RUNNING lt 0 1 gt MP gt EMERGENCY STOP OK lt 0 1 gt MP gt PUSH BUTTON READY lt 0 1 gt MP gt PUSH BUTTON MOTION OFF lt 0 1 gt MP gt PUSH BUTTON MOTION ON lt 0 1 gt MP gt ROLL SENSOR FAIL lt 0 1 gt MP gt PITCH SENSOR FAIL Page 0900 M SIM CONTROL INPUT ACCESS lt 0 1 gt SET LOADED SHIP preset condition lt 0 1 gt SET UNLOADED SHIP preset condition lt 0 1 gt BOILER ISOLATION lt 0 1 gt IG ISOLATION lt 0 1 gt ACTIVATE MOTION PLATFORM 1 CHT2000 VLCC II ws Variable List Page 93 N E o 7 07020 02247 02447 02647 03047 03247 HP Z Q gt 9 Z Z r ATT m Q m m 9 Q gt
172. ed together with tag no tag name engineering units and upper lower limits for alarms The limits can be altered from Instructor mode by point and click with centre tracker ball button at limit and then type in new value press Enter Carriage Return Page 5 15 5 2 3 5 2 3 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Function buttons at the Operator section This section comprises all remedies for the student to conduct an exercise independent on the Instructor or other students From this section the student has access to the Malfunction List Variable List Alarm List Picture Directory and other useful features The following pages contain information on how to utilise these functions Malfunction List Most of the Model Drawings comprises one or more buttons marked M By clicking at one of these buttons with the centre push button of the tracker ball a new window will appear at the monitor containing the Malfunction List directory The M buttons turn yellow when malfunctions are activated in Instructor mode only When in operator mode student all malfunctions are displayed but there is no indication of which fault is introduced In instructor mode the same window shows active malfunctions and in addition their settings Malfunctions are activated by the left hand side push button of the tracker ball while resetting of malfunctions introduced is carried out by use of the right hand side push button
173. eed Surge Control In Speed Surge Control mode the pump speed set point is limited automatically by the liquid level in the oil gas separator Le When the liquid level is reduced the pump speed set point is reduced accordingly over riding the manual speed setting Flow Surge Control In Flow Surge Control mode the discharge valve opening is adjusted automatically by the pump suction pressure in the oil gas separator I e When the pump suction pressure drops the discharge valve opening is reduced accordingly over riding the manual speed setting The Speed Surge Control and the Flow Surge Control can be set simultaneously Tripping If certain critical conditions occur the pump will trip 1 the pump turbine steam supply valve is automatically closed The pump will consequently loose its power and stop after a while Alarm will be given Reset Trip Before the pump can be re started the trip has to be reset Trip Causes The cause for the trip may be printed out on paper and it can be identified on the VDU display The trip causes are No 1 Overspeed No 2 Pressure low No 3 Temperature high No 4 Discharge pressure high No 5 Inert gas pressure low low cargo pumps only CHT2000 VLCC II ws User s Manual Page 4 71 Doc no SO 0603 A 9 January 1997 4 8 1 Ballast Water Pump uas Ballast Water Pump mae n TURBI PUMP Efficiency 2236 41 tbe Pesar Shaft
174. ending moment and deflection for a ship s hull is rather complex and will require a computer program The DataLoad programs included in the CHT2000 will continuously i e approx each 10th second compute the parameters said on the current load condition related the ship s geometry and the hull s strength as stated in the computerised ship model of the Det norske Veritas DnV CHT2000 VLCC II ws User s Manual Page 4 38 Doc no SO 0603 A 9 January 1997 4 4 Computerised Load Master 501 Bargraph Load 502 Cargo Survey Load Master L 503 Shear Force Load 504 BendigMoment Load Master 505 Load Master 506 Stability Curve LoadMastt pf 100 Directory 1 CHT2000 VLCC II ws User s Manual Page 4 39 Doc no SO 0603 A 9 January 1997 The purpose of the Computerised Load Master is to avoid excessive bending stresses in the hull structure These stresses vary with the cargo distribution throughout the length of the ship Incorrect loading can damage the ship and hence the cargo ballast must be placed according to a carefully calculated plan It is however impossible to foresee all possible cargo distributions It is therefore necessary to have an easy to handle computer on board which can calculate all the appropriate stresses for every load distribution case In addition to t
175. er line tot flow 68 08 M3vh Dil H 0 00 concent 0 00 168 00 100 09 100 08 108 08 168 08 S P cops coP2 68 08 to Bottom line 3 CHT2000 ULCC II REV 1 2 CHT2000 VLCC II ws User s Manual Page 5 86 5 7 10 5 7 11 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The slop consists of mixed oil and dirty water Slop The slop tanks are used to segregate these two fluids from each other Double Slop Tank System The slop tanks are arranged in a double tank system where the port slop tank is the primary slop and the starboard slop tank is the secondary slop The system works on the following principles The mixture of oil and dirty water is pumped to the port slop tank for main separation When the oil and water has separated the oil is on top and the water on bottom The water which has settled out can be decanted to the starboard slop tank When the water in the starboard slop tank is pumped overboard the content in the Overboard Discharge Line can be manually inspected In addition it is automatically monitored by the ODM Page 5 87 5 7 12 5 7 13 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Filling the Port Slop Tank Before a mixture of oil and water is pumped into the port slop tank it is necessary that there is clean water in the suction piece of the slop decanting line between the po
176. for centrifugal type pumps Close the discharging valve Open the suction valve Fill the pump with liquid oil water Start the pump Open the discharging valve Page 5 70 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 This page is intentionally left blank Page 5 71 Doc no SO 0603 A 16 03 00 01 45 42 Picture Alarm Ballast Water Pump BA 199 PUMP Efficiency 2218 41 kWh kg Power 2549 9 Shaft 0111 70 Efficiency 264 16 Index 26 66 x Shaft speed H1300 1 rpm P9 73 Valve 4 100 0 115 C22 ake Ctr ballast i U 180 00 line Speed 4 1900 Ctr Speed 1966 1A 268 Steam B W Pump START STOP Tripped RESET Trip Prim P 5 ballast line CHT2888 ULCC II REV 1 2 CHT2000 VLCC II ws User s Manual Page 5 72 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Pump Speed The set point of the pump turbine governor which regulates the pump speed is controlled by clicking on the Speed control and entering the new set point Open Close The discharge valve setting is controlled by means of entering the new value 0 100 The pump flow and the pump pressure is controlled by the pump speed setting and the discharge valve setting High bearing temp Running of the pump at a substantial speed against a high discharge pressure may cause high bearing temperature after a certain per
177. ge 5 31 Doc no SO 0603 A 16 03 00 01 35 16 Picture Load Discharge Ballast Routing NOR i i V V p 1 j 1 1 1 1 1 1 1 1 57575757 V V V 103 gt lt V Line 4 gt 5 3 gt gt gt p e us 01 10 Ballast line E Line 2 kv gt r pij pij p p Line 1 H pj SJ gt slop X over DH ILI gt CHT2000 ULCC II REV 1 2 CHT2000 VLCC II ws User s Manual Page 5 32 5 3 3 13 5 3 3 14 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Deck Valves The deck valves are modelled as on off valves and are operated by an OPEN and CLOSE clicking on the symbol The manifold shore connection can only be connected from the Instructor mode picture MD 107 108 and 111 114 Cargo pumps and discharge valves The cargo pumps and ballast pump are of the centrifugal type pumps All pumps are operated from the Individual pump picture MD 211 215 Trip The pumps may trip if one or more of the following conditions are present Steam supply pressure is too low Condenser pressure is high Inert Gas pressure is low cargo pumps only Bearing lub oil pressure to low Bearing lub oil temp to high These conditions can be set by the engineer 1 6 the instr
178. h m3 h bar degC bar degC FLOW FROM BOTTOM LINE 2 FLOW FROM SW SUCTION CROSSOVER FLOW FROM CO SUCTION CROSSOVER TOTAL FLOW FROM TANK WT 1 S TOTAL FLOW FROM TANK WT 1 P TOTAL FLOW FROM TANK CT 4 CROSS FLOW FROM BLIN3 PIPE LINE 2 PRESS aft PIPE LINE 2 TEMP aft PIPE LINE 2 OIL CONTENT aft PIPE LINE 2 PRESS fore PIPE LINE 2 TEMP fore PIPE LINE 2 OIL CONTENT fore CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 21 0025 M CARGO LINE 2 DECK PIPING A 602340 m3 h FLOW FROM COP2 TO DECK LINE 02356 m3 h FLOW FROM COP2 TO TC COW CROSSOVER D 002357 m3 h FLOW FROM COP2 TO SLOP CROSSOVER E F 602341 m3 h LOAD FLOW to bottom line 2 G02343 m3 h FLOW FROM SHORE TO MANIFOLD 2 H I 2346 bar DECK LINE 2 PRESSURE aft J T02347 degC DECK LINE 2 TEMPERATURE K X02350 DECK LINE 2 OIL CONTENT aft L 2351 bar MANIFOLD 2 PRESSURE N T02352 degC MANIFOLD 2 TEMPERATURE 02353 MANIFOLD 2 OIL CONTENT 202354 kg m3 MANIFOLD OIL DENSITY Q R 5 2 22 Page 0026 M CARGO LINE 2 PUMP MONITOR PAGE A B C T03740 hour TOTAL PUMP RUNNING TIME D M03741 ktonn TOTAL PUMP FLOW MASS E E03742 MWh TOTAL COP2 ENERGY F G H M03743 tonn TOTAL TURBINE STEAM MASS I Z03744 US TOTAL STEAM COST J K L 5 CHT2000 VLCC II ws Variable List Page 13 2 23 C02460 C0
179. he Electrical Power Plant will be printed If connected Malfunction Setting and Resetting of Malfunctions Instructor Not in use Log printer 2 For future use Log printer 3 For future use Page 5 8 5 2 1 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Snapshot A snapshot represents the condition of the simulation at the time it was created If the student fails to run the simulation properly and for instance this results in a black out or any other abnormal condition the situation can be corrected by simply retrieve a snapshot prior to the accident Each Snapshot is identified by the time it was created manually or automatically When generated automatically the interval between each snapshot has to be specified See also description of Snapshot push button Malfunction Editor Gives ability for editing and creating of malfunctions prior to start or during the simulation It is a prerequisite that a scenario is loaded into the workstation To create a malfunction click on software button CREATE and click at one of the buttons 01 to M40 and type descriptive name of the malfunction IMPORTANT When a malfunction name has been typed and ENTERED a prompt will ask you which TAG name from the Malfunction List is wanted This tag name must be written with full style name and number directly copied from Malfunction List In addition type in S Otherwise tag will not enter When prompt changes colour
180. he current data on draft trim and heel the Load Master also calculates the following based on manual input Hydrostatic conditions draft trim Intact stability FS GM GZ Meta Centric height Longitudinal strain shear force bending moment hull deflection Relative tank content The output from the Load Master is displayed on the variable pages The shear force bending moment hull deflection and stability curve can be screen dumped to the printer CHT2000 VLCC II ws User s Manual Page 4 40 Doc no SO 0603 A 9 January 1997 4 5 Model Description 101 Cargo Bargraph pose Wing Tank 4 Port Condition 102 Cargo Survey Wing Tank 5 Port Condition Shear For Wing Tank 6 Port Condition Bending Moment 13 Center Tank 4 Atmosphere Stabili i 13 Center Tank 1 Atmosphere 1 Wing Tank 1 Stb Condition Deflection Wing Tank 2 Stb Condition Wing Tank 1 Port Atmosphere 2 Atmosphere 3 Atmosphere 0 tability Curve Wing Tank 4 Stb Condition 227 Wing Tank 2 Port Atmosphere 0 Load Discharge Wing Tank 5 Stb Condition 228 Wing Tank 4 Port Atmosphere 0 Cargo Deck Line 5 Wing Tank 6 Stb Condition 229 Wing Tank 5 Port Atmosphere 0 Cargo Pump Room Bunkers and Water Bargraphs 12 1 12 1 13 1 13 1 13 1 13 1 20 Wing Tank 6 Port Atmosphere Cargo Bottom Lines 20 Load Discharge Ballast Routing 20 20 2 Stb Atmosphere Stb Atmosphere Stb Atmosphere 1 1 1 1 1 1 1 1 1 11
181. he final stripping of all cargo tanks Always carry out 100 COW of all cargo tanks if permission granted by receivers or instructed by Charterers This procedure allows free flow of liquid cargo to the suction bell mouths and also prevent blockage through build up of sediment sludge If dirty ballast is filled prior to departure completion of discharge the Student must make sure that the tanks where dirty ballast is filled are stripped and completely dry All cargo lines and cargo pumps containing cargo are to be stripped drained completely dry before filling ballast Page 5 59 Doc no SO 0603 A 16 03 00 61 53 52 Picture Alarm Running HD 222 Center Tank 1 Atmosphere Center Tank 1 Condition 122 188 GAS FLOW Inert inlet 6 1462 0 m h INERT GAS DECK LINE 0 gt 5 1 59 Ax HC 5 51 X Pressure 0 Abar TANK ATMOSPHERE 0 gt 5 1 68 A HC 36 62 7 Pressure P0 03 fbar MISC TANK DATA Volume 87 13 Dens oil 0 819 99 Dens water D 1025 0 L Disch Rate 6 2924 5 Liq Content 21542 full kg m kg m msyh tonnes CHT2000 VLCC II ws User s Manual B flammable mixture 25 20 15 HC Z Chydro carbon 10 0 Z 10 Coxygen CHT2000 ULCC II REV 1 3 Page 5 60 5 6 5 6 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inerting Procedures General Inert Gas is a non inflammable gas such as CO or tha
182. he leakage of air into inerted tanks or of Inert Gas into tanks which are being gas freed Page 5 66 5 6 10 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inert Gas Emergency Procedure In the event of Inert Gas system failure such as Inability to deliver the required quantity and or quality of Inert Gas Inability to maintain required pressure in the cargo tanks Shut down of the Inert Gas plant Immediate action must be taken to prevent any air being drawn into the tanks All discharging deballasting or tank washing must cease and Inert Gas main deck isolating valve must be closed Cargo operations must not resume until the Inert Gas plant is returned to service and the tanks are satisfactorily inerted Page 5 67 Doc no SO 0603 A 16 03 00 P0 00 V V 5 V V V H U3 24 123 01 37 125 8 52 123 183 WT3P 169 00 A FPT 11690 00 A H tank top H tank top 025 25 overf low 026 00 overflow 1 68 98 8784 68 9922 929 B W P 1 8 86 8 P0 89 P1 86 9 98 P0 05 phy 2 pkg 924 8 8 1 8 8 6 188 8 1 8 ED G 784 7 to Cargo tank top Survey overf low 1560 00 A 1 6784 53 REV 1 3 CHT2000 VLCC II ws User s Manual Page 5 68 5 7 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Ballasting is a proce
183. he student using it will act as his own instructor meaning that he will have the instructoris privilege to start pause the simulation Each individual can run the exercise at his own pace CHT2000 VLCC II ws User s Manual Page 4 4 Doc no SO 0603 A 9 January 1997 The pushbuttons on the operational keyboard are grouped together in logically arranged clusters All the instructor functions are located on the left side of the keyboard The keyboards have a key with which the instructor can prohibit student s access to the instructor functions on the keyboard The following pages comprises a functional description of the main cargo handling systems and related sub systems The process diagrams with corresponding information such as temperature flow pressure set points etc are presented on the colour graphic workstation Additional diagrams and information giving insight to the simulated models are available and can be addressed by using the functional keyboard The Process Diagrams presented have the following colour code for pipelines Light Blue Steam Blue Fresh Water Green Sea Water Yellow Diesel Oil Brown Fuel Oil Orange Cargo Pink Vapour The Cargo lines have the following colour code Green Line no 1 Yellow Line no 2 Brown Line no 3 Red Line no 4 CHT2000 VLCC II ws User s Manual Page 4 5 Doc no SO 0603 A 9 January 1997 The Process Diagrams comprises abbreviations such as
184. in when time limits entered are reached Activated this button will make fault go on and off repeatedly within specified time limits as long as scenario is run CHT2000 VLCC II ws User s Manual Page 4 16 Doc no SO 0603 A 9 January 1997 When activated time ramp for fault to develop be specified Common for all four function buttons are that faults can be simulated after entering a scenario only when buttons are activated When active buttons change colour Ramp function can be active together with any of three other buttons To activate click on buttons with centre trackerball button On the bottom half of screen buttons 41 to 80 is event malfunctions Used and created as malfunction but triggering actions instead of malfunctions Such as closing of valves CHT2000 VLCC II ws User s Manual Page 4 17 Doc no SO 0603 A 9 January 1997 INSTRUCTOR n 11 INIT COND OPERATION SCENARIO DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE Action Editor Allows editing of actions i e somebody stopping a pump unintentionally Active in instructor mode only Using and creating actions as malfunction editor Input of tag names similar to malfunctions editor adding period S or underscore S after tag When starting a scenario wanted malfunctions and action to be performed d
185. incl residues K M01203 tonn WT4S TOTAL TANK MASS incl residues L M01303 tonn WT4P TOTAL TANK MASS incl residues M M01403 tonn CT4 TOTAL TANK MASS incl residues N M01503 tonn WTSS TOTAL TANK MASS incl residues 01603 tonn WTSP TOTAL TANK MASS incl residues P M01703 tonn WT6S TOTAL TANK MASS incl residues Q M02003 tonn WT6P TOTAL TANK MASS incl residues R M04111 tonn FORE HFO TANK MASS T M04121 tonn AFT HFO TANK MASS Page 76 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 153 Page 0502 M TANK SURVEY VOLUMES A 00001 m3 FPT TOTAL TANK LIQUID VOLUME 00101 m3 CT1 TOTAL TANK LIQUID VOLUME 00201 m3 WT1S TOTAL TANK LIQUID VOLUME D 00301 m3 WTIP TOTAL TANK LIQUID VOLUME E V00401 m3 CT2 TOTAL TANK LIQUID VOLUME F V00501 m3 WT2S TOTAL TANK LIQUID VOLUME G V00601 m3 WT2P TOTAL TANK LIQUID VOLUME H V00701 m3 WT3BS TOTAL TANK LIQUID VOLUME I V01001 m3 WT3BP TOTAL TANK LIQUID VOLUME J V01101 m3 CT3 TOTAL TANK LIQUID VOLUME K V01201 m3 WT4S TOTAL TANK LIQUID VOLUME L V01301 m3 WT4P TOTAL TANK LIQUID VOLUME V01401 m3 CT4 TOTAL TANK LIQUID VOLUME N V01301 m3 WTSS TOTAL TANK LIQUID VOLUME 01601 m3 WTSP TOTAL TANK LIQUID VOLUME P V01701 m3 WT6S TOTAL TANK LIQUID VOLUME Q V02001 m3 WT6P TOTAL TANK LIQUID VOLUME R S T 2 154 Page 0503 M TANK SURVEY RELATIVE VOLUMES 00002 FPT TANK VOLUME cap 12113 m3 00102 9
186. ing can commence The loading operation shall commence at reduced rate The line up should then be checked by Ensuring that the cargo is flowing into correct tank s Ensuring that cargo is not flowing into incorrect tanks Ensuring that there is no leaks in the valve or piping After these checks have been made and found satisfactory the vessel may inform the Terminal to increase the flow to agreed full loading rate CHT2000 VLCC II ws User s Manual Page 5 50 5 4 9 5 4 10 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Monitoring Cargo Tanks The ullage of the tanks being loaded should be frequently and regularly monitored especially when approaching the topping off range Cargo temperature should be taken both at beginning and end of loading Changing Tanks Extra care should be exercised to avoid over pressuring the ships and shore lines by closing too many valves against the shore pressure When topping off special care should be exercised and the rate of flow reduced to the actual tank The following points should be considered when topping off tanks Closing off one tank increases the rate of flow to other open tanks on the same line As the vessel trims by stern the rate of flow into open aft tanks will increase The rate of flow into any tank which is nearly full can quickly be reduced by opening the valve to an empty tank on the same line This procedure in conjunction with closing
187. interference with the others Independent of what simulation mode is used the workstations need access to the harddisk Figure 1 2 Simulator Concepts CHT2000 VLCC II ws User s Manual Page 1 6 Doc no SO 0603 A 9 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Chapter 2 Technical Specification CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 9 January 1997 2 TECHNICAL SPECIFICATION 2 1 Workstation HP 9000 425e The Hewlett Packard Workstations has the following specifications HP 9000 425e Workstation MC68040 CPU Clock 25 Mhz EE O 16Mb ECC RAM Error Control Correction 16 Colour monitor Resolution 1280 1024 SCSI and LAN Both plus 1 RS 232 Interface Performance 22 MIPS Million Instructions pr sec 2 6 MFLOPS Million floating point operations pr sec All data according to HP technical specification 2 2 Server HP C 3020 T The Host Computer mathematical model computer is a Hewlett Packard server Together with distributed microprocessors it forms the complete trainer computer system The microprocessors are located in workstatios and intelligently interfaced to the Host Computer via Ethernet 1 0 Gb SCSL 2 0 Gb Digital Data Storage Tape All data according to HP technical specification CHT2000 VLCC II ws User s Manual Page 2 1 Doc no SO 0603 A 9 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Chapter 3 Installation CHT2000 VLCC II ws Use
188. iod of time even if the discharge valve is equipped with a recirculating release valve The performance of the pump turbine is dependent on the steam supply pressure and temperature as well as the condenser vacuum These parameters will vary with the pump turbine load Page 5 73 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The pump trip is indicated by a flashing light on the pump control section Before the pump can be re started the trip has to be reset This is done by clicking the reset symbol after the pump has stopped The flashing light in the pump control section will then extinguish if the cause for the trip has disappeared or turn to steady light if the cause for the trip still is present This can then be reminded by the engineer i e the instructor Reset trip Trip Causes The cause for the trip may be printed out on the instructor s printer and it can be identified on the display and on the instructor s VDU The trip causes are Overspeed Lub oil pressure low Bearing temp high Discharge pressure high Stopping The pump is stopped by clicking the STOP symbol The turbine steam supply valve is closed and the pump is brought to stop after a while Page 5 74 5 7 2 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Segregated Ballast The Segregated Ballast Tanks SBT are completely separate from the cargo oil and fuel system and are permanently allocated
189. ion 9 section 10 section 11 section 12 Page 0601 M HULL BENDING MOMENTS ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm ktonm L 700 0 L 300 0 L 350 0 L 500 0 L 700 0 L 700 0 L 700 0 L 700 0 L 700 0 L 500 0 L 200 0 L 200 0 L 700 0 H 700 0 BENDING MOMENT section 0 H 300 0 BENDING MOMENT section 1 H 350 0 BENDING MOMENT section 2 H 500 0 BENDING MOMENT section 3 H 700 0 BENDING MOMENT section 4 H 700 0 BENDING MOMENT section 5 H 700 0 BENDING MOMENT section 6 H 700 0 BENDING MOMENT section 7 H 700 0 BENDING MOMENT section 8 H 500 0 BENDING MOMENT section 9 H 200 0 BENDING MOMENT section 10 H 200 0 BENDING MOMENT section 11 H 700 0 BENDING MOMENT section 12 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 165 Page 0602 M HULL DEFLECTIONS A L06040 HULL DEFLECTION section 0 106041 m HULL DEFLECTION section 1 D L06042 m HULL DEFLECTION section 2 106043 HULL DEFLECTION section 3 106044 m HULL DEFLECTION section 4 G L06045 HULL DEFLECTION section 5 H L06046 m HULL DEFLECTION section 6 I L06047 m HULL DEFLECTION section 7 J L06050 m HULL DEFLECTION section 8 K L06051 m HULL DEFLECTION section 9 L L06052 m HULL DEFLECTION section 10 1 06053 m HULL DEFLECTION section 11 N L06
190. l SOUNDING even keel CLEAN OIL INTERFACE LEVEL CLEAN WTR INTERFACE LEVEL OIL CONTENT IN WTR OIL MIXTURE TOTAL TANK MASS incl residues TANK VOLUME cap 30818 m3 CLEAN OIL MASS DIRTY OIL MASS DIRTY WATER MASS CLEAN WATER MASS HARD RESIDUES SOFT RESIDUES DRIP RESIDUES OIL DENSITY at 15 dgrC WTR DENSITY at 15 dgrC CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 2 85 0204 M CARGO TANK CT 2 HEATING A B C 00453 degC 1 40 0 H 100 0 CT2 CARGO TEMPERATURE E V00456 96 CT2 CARGO HEATING STEAM VALVE 000457 m3 h CT2 CARGO HEATING STEAM FLOW H I 00460 kW CT2 HEAT FROM STEAM J E00454 kW CT2 HEAT LOSS SEA AIR K E00455 kW CT2 HEAT LOSS TO ADJACENT TANKS L M N O P Q R S T 2 86 Page 0205 M CARGO TANK 2 MISCELLANEOUS A 700472 lt 0 2 gt CT2 IG INITIATION 2 IG C D P00426 bar L 0 1 H 0 1 CT2 TANK ATMOSPHERIC PRESSURE F X00427 L 0 0 8 0 CT2 OXYGEN CONTENT G X00430 CT2 HYDRO CARBON CONTENT H M00431 CT2 INERT GAS MASS 02 CO2 N2 J M00432 kg CT2 HYDRO CARBON MASS K L 00445 bar CT2 LIQUID GAS PRESSURE 446 CT2 GEODETIC PRESSURE N P00447 bar CT2 TOTAL TANK BOTTOM PRESSURE O P Z00468 DEG CT2 TANK CLEANING UPPER LIMIT Q Z00469 DEG CT2 TANK CLEANING LOWER LIMIT R S T CHT2000 VLCC II ws Variable List Page 45 2 87 og 000512 L00511 U00
191. la Ir MT L This can be found in the hydrostatics tables CHT2000 VLCC II ws User s Manual Page 4 31 Doc no SO 0603 A 9 January 1997 Heel The heel is adjusted until the heeling moment is equalised by the buoyancy moment of the displaced water The heeling will always take place along the longitudinal centre line LCF dx Water plane area L L Aw dAw B x dx 0 0 Water plane moment of area longitudinal L L FL xdAw B x x dx 0 0 Water moment of inertia longitudinal L L IL x2dAw B x x2 dx 0 0 CHT2000 VLCC II ws User s Manual Page 4 32 Doc no SO 0603 A 9 January 1997 Intact Stability As long as the vessel lies in upright position there will always be an equilibrium between the weight forces light ship cargo acting through the gravity centre G and the total buoyancy forces acting through the buoyancy centre B G and B will always be located on the same vertical line at a distance of KG and KB from the keel respectively When the ship is inclined due to a heeling moment the buoyancy centre will move to a new position due to the change in displacement s volume and shape The vertical line through b will cut the ship centre line at an angle 0 in the point At small angles of heeling point M is called the Initial Meta Centre CHT2000 VLCC II ws User s Manual Page 4 33 Doc no SO 0603 A 9 January 1997 The horizontal dis
192. lar requirement stipulated in the voyage orders Page 5 42 5 4 2 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Planning Cargo Stowage In planning the stowage of the cargo the following considerations should be taken into account The limiting zone of the laden voyage is to be determined by zone charts encountered and estimated fuel consumption on planned passage The final freeboard should be in compliance with the applicable load line zone with allowance for voyage consumption of bunker the F W allowance and deflection The sailing condition should be within the maximum permissible limits of bending and shear force moments for sea condition If the proposed voyage is to or through warmer areas sufficient volume should be left in the tanks to allow for possible expansion of cargo There should be two valves between segregated cargo parcels The sailing trim should ensure that the vessel arrives at the discharge port on even keel draft Tanks should be allocated to different grades to enable the vessel to trim sufficiently for efficient discharge and draining of tanks and efficient scheduling of discharge COW and stripping One tank should be designated the last tank of loading This is usually a centre tank at the trimming centre of the vessel Page 5 43 Doc no SO 0603 A 16 03 00 Alarm 90 00 32 Picture 1 Cargo Survey inn TAE Running HD 102 PORT l
193. lated from the variable page no 0081 Steam boiler control data This will allow all aux systems to operate without the boiler active CHT2000 VLCC II ws User s Manual Page 4 64 4 5 24 81 33 50 Doc no SO 0603 A 9 January 1997 Inert Gas Plant Picture ns 203 Inert Gas Plant vaa mon BOILER terp Flow T 368 00 612017 TO EEC MATER SER pressure P0 93 A 89 X 1 63 ARES 0 Xi A HRIH LINK pressure P 63 A he 2 21 0 X1 84 A en ator tro Fir gt Fa pan fron de e 1 1 3 UNIT CONVERSION PRINT REPORT The cargo handling simulator is modelled with a steam boiler where flue gas is taken from the boiler uptake and directed through the scrubber fans and deck water seal to the main inert gas deck line The capacity of the inert gas plant is approximately 40 000 cbm h provided sufficient flue gas is available from the boiler Flue gas is produced by steam consumption to aux systems The scrubber washes and cools the flue gas in order to reduce soot and SO content The oxygen content will variate with the boiler load In order to avoid O exceeding 5 to enter the tank an automatic valve will close and route the fluegas to the funnel Another valve controlling the mainline pressure will also regulate the flow to the tanks by bypassing to the funnel F
194. le press the select button at the unit and type the new value and terminate by pressing Enter Carriage Return Page 5 17 5 2 3 3 5 2 3 4 5 2 3 5 5 2 3 6 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The Alarm List contains alarm groups displaying information of actual value alarm limits and alarm status After recognition of the desired Alarm group in the Alarm group directory use the select button to display the desired alarm group List can be scrolled moved or removed with cursor and centre tracker ball button to find desired alarm Alarm List After having pressed the ALARM LIST and identified the sub system window with list of alarms will be displayed Picture Directory Displays the directory of all Model Drawings MD s After recognition of system click with the centre tracker ball push button on the actual Model Drawing and seconds later the subsystem is displayed on the screen Mark Picture When pressing Mark Picture the displayed Model drawing can be saved and easily recalled by using the Recall Marked Picture push button After clicking Mark Picture enter a chosen number between O and 9 After clicking Recall Marked Picture followed by the same number the previously MD is displayed again Select Picture Page 5 18 5 2 3 7 5 2 3 8 5 2 3 9 5 2 3 10 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Allows selection of a Model Drawing after typing M
195. ll button will allow entering rate of wear for component Selecting 100 rate of wear will render component useless instantaneously When a fault is selected ON the system picture will have the M button in lower left corner lighted in yellow Student in operator mode will not have this indication of active faults Variable List Displays window with list of variables directory After recognising main system clicking on system button displays list of variables for this system List can be scrolled moved or removed with centre button on trackerball and cursor Instructor After pushing VARIABLE LIST identify sub system and press selected system Displayed window will then be identical to that mentioned in alarm pages Tag details and measured values will be displayed Displayed data can be changed after clicking on values with centre trackerball button After typing in new values and pressing enter new data entered will gradually return to measured values Selecting upper lower alarm limits and entering new data will permanently reset limits CHT2000 VLCC II ws User s Manual Page 4 24 Doc no SO 0603 A 9 January 1997 MALFUNC VARIABLE ALARM LIST LIST LIST PICTURE MARK PREVIOUS DIRECTORY PICTURE PICTURE SELECT RECALL NEXT PICTURE MARKED P PICTURE ALARM ALARM ALARM ACKN LOG SILENCE Operator Read only no actions or changes possible Alarm List Displays window with alarm page directory After recognition of
196. low Gravity Flow The gravity flow is generated by opening the valves between two or more tanks with different liquid levels opening of manifolds when connected and by opening seachest in the ballast system A flow will then start from the tank with the higher level to the tank with lower level and for ballast according to draught The flow rate will depend on The difference between the actual tank levels The flow resistance caused by pipe characteristics Valve characteristics and valve setting The flow will continue as long as a difference in tank levels is present The tank levels will change according to the flow rate and the tank discharging valve s When ballasting the flow will continue until the draught and the level in the ballast tanks equalise Page 5 27 Doc no SO 0603 A 16 03 00 Alarm Group 66 29 14 Picture 1 Cargo Bottom Lines ev m n Bot line Bot line 1 131 135 116 CHT2000 ULCC II REV 1 2 Page 5 28 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 5 3 3 6 Pump Flow The pump flow is generated by opening the suction valve s starting the pump and opening the discharge valve s The flow rate will depend on The pump speed The flow resistance caused by pipe characteristics Valve characteristics and valve settings The suction head cavitation The liquid density 5 3 3 7 Cargo Ballast
197. m Strip Oil Gas 5 82 Linestpp 3 83 sy 5 87 Double Slop Tank 5 87 Filling the Port Slop Tank 3 88 Separation in the Port Slop Tank eet e iret o ardens 5 88 Decanting the Port Slop Tank 5 89 Oil Discharge Monitor Ne 5 90 Oil Discharge Monitoring Variables pp 5 91 Iner np and 5 93 5 94 Shit LO Wil PROC OCI 5 95 5 95 Inert Press Q COMENG 5 95 MEE 5 99 CHT2000 VLCC II ws User s Manual Page iv Doc no SO 0603 A 9 January 1997 5 8 6 Tank Atmosphere Pressure Control 5 99 5 9 Tank Cleaning Water gt 5 99 5 9 1 Crude Oil Washing COW a 5 101 CHT2000 VLCC II ws User s Manual Page v Doc no SO 0603 A 9 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Chapter 1 Introduction CHT2000 VLCC II ws User s Manual H Doc no SO 0603 A 9 January 1997 1 INTRODUCTION The last few years have seen the beginning of a drastic change in the education of ships officers Due to new
198. m m 9 Q Z gt X03600 ARAHVOZ X03601 CHT2000 VLCC II ws Variable List Doc no SO 0606 A January 6 1997 Page 0062 M EDUCTOR m3 h m3 h m3 h lt 0 1 gt bar bar bar lt 0 1 gt m3 h EDUCTOR DRIVE FLOW EDUCTOR SUCTION FLOW EDUCTOR DISCHARGE FLOW EDUCTOR DRIVE VALVE EDUCTOR SUCTION VALVE EDUCTOR DRIVE PRESSURE TC COW CROSSOVER PRESSURE CO SUCTION CROSSOVER PRESSURE EDUCTOR DISCHARGE FLOW OIL CONTENT TC COW CROSSOVER OIL CONTENT CO SUCTION CROSSOVER OIL CONTENT TCOWC COSC CONNECTION VALVE FLOW FROM TCOWC TO COSC Page 0064 M OIL DISCHARGE MONITOR SLOPC lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt m3 h m3 h m3 h ppm ppm M03603 kg M03604 kg Nm L 0 0 20 0 ppm L 0 0 H 15 0 OIL DISCHARGE MONITOR AUTO SWITCH OIL DISCHARGE MONITOR RESET COMMAND OVERBOARD AUTO VALVE RECIRC TO SLOPT AUTO VALVE OVERBOARD VALVE high discharge SLOPT P DIRTY BALLAST INLET VALVE SLOP CROSSOVER PRESSURE FLOW OVERBOARD high discharge DIRTY BALLAST DISCHARGE TO SLOPT P FLOW FROM SLOPC TO ODM SLOP CROSSOVER OIL CONTENT OVERBOARD OIL CONTENT TOTAL OVER BOARD DISCHARGED OIL MASS SPECIFIC OIL DISCHARGE RECIRC OIL CONTENT LIMIT Page 27 Doc no SO 0604 A January 6 1997 2 51 0065 M SMALL DIAMETER LINE A B C V03320 0 1 SMALL DIAM LINE MANIF VALVE S D V03321 0 1 SMALL DIAM LINE MANIF VALVE
199. mulator response time constant for tank levels Choose between three levels slow to very fast CHT2000 VLCC II ws User s Manual Page 4 12 Doc no SO 0603 A 9 January 1997 INSTRUCTOR 11 OPERATOR INIT COND OPERATION SCENARIO DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE Dynamic response Sets simulator time response constant for controllers Ship dynamics Will change ship dynamic response time constant Log printer 1 Determines which events or alarms to be logged on printer All five buttons can be activated simultaneously Snapshot column Whenever simulator creates a simulation snapshot this will be placed here for later retrieval Snapshots enter under a button with inserted time when snapshot was made Snapshots can be auto generated with push button snapshot intervals When pushed page will prompt for intervals between snapshots Note Snapshot will only be visible when the simulation is started from the same initial conditions Malfunction Editor Allows editing of malfunctions during simulation CHT2000 VLCC II ws User s Manual Page 4 13 Doc no SO 0603 A 9 January 1997 Only possible from INSTRUCTOR CHT2000 VLCC II ws User s Manual Page 4 14 Doc no SO 0603 A 9 January 1997 Instructor A scenario with an initial condition must be available and chosen This
200. nd discharging will be shown in detail to the operator There are installed a washing machine in each tank that can be programmed from MD 220 The washing machines are strategically placed in order to minimise shadow effect Steam heating coils are fitted in the bottom of each tank and is operated by the cargo heating steam valve 4 5 18 Wing Tank 1 2 4 5 amp 6 Port Condition The tank facilities is the same for port wing tanks as described for centre tanks 4 5 19 Wing Tank 1 2 4 5 amp 6 Stb Condition The tank facilities are the same for starboard wing tanks as described for centre tanks CHT2000 VLCC II ws User s Manual Page 4 58 Doc no SO 0603 A 9 January 1997 4 5 20 Bunkers and Water Bargraph 01 34 05 Picture Alarm Running HD 201 Bunkers and Water Bargraphs Group 0 0 Storage 0 0 fresh ti H r o 181 F 0 water ps To uL NM id serv H F 0 H F D serv setl WATER DIESEL OIL TANKS HEAVY FUEL OIL TANKS X full 995 88 935 08 935 08 95 8 093 35 993 75 100 80 50 40 20 fresh water D O serv D O 0 0 storage H F O serv HF O aft H F O 1425 0 M95 00 M1u2 58 M 388 80 2387 1 TOTAL TOTAL TOTAL Fresh water H1425 0tonnes Diesel oil 205 00tonnes Heavy fuel oil 6509 6tonnes C
201. ns and the corresponding Buoyancy forms The graphic picture will display three different curves The yellow curve shows maximum permitted shear forces in harbour condition The red curve shows the maximum permitted shear forces in seagoing condition The blue curve shows actual shear forces The shear forces P in each section 0 12 is expressed in Kilotonnes Each value is equipped with an alarm that activates when the limit value is exceeded The frame number is identical to the distance from aft perpendicular to tank section in meters CHT2000 VLCC II ws User s Manual Page 4 46 Doc no SO 0603 A 9 January 1997 4 5 4 Bending Moment 00 04 15 Picture Alarm Running 104 Bending Moment Group HEEL CONDITION DEADWEIGHT DRAUGHT meter NE TRIM T 4 Sea Density D 1025 0 1888 ton 180 80 Aft L 18 51 3 Sea temp 25 00 C of V 96 17 Mid STBD L 18 30 E 2 summer mark Mid PORT L 18 30 rr Es DISPLRCEHENT STRBILITY meter Fud L 18 03 1888 ton 210 35 GM Corr 15 50 Trim E043 2 2 FS Red 19 72 1 1 0 00 X0 00 5 5 X0 08 n 5 OS Rad 14 91 B zd 1 Limits Harbour Open sea 103 Q 180 1 0 332 7 A A 0 335 4 A Q 152 2 A ton Q 136 4 0 2 0 349 8 9 308 7 A Q 290 4 A Q 116 4 A meter TT H T T I T I X
202. of masses Clean oil on the top Dirty oil dirty water emulsion in middle Water on the bottom The settling process will be speeded up when The difference in specific gravity is increased The tank temperature is increased The mixing process will be intensified when The ship s speed is increased The roughness in the weather is increased The input flow to the tank is increased CHT2000 VLCC II ws User s Manual Page 4 77 Doc no SO 0603 A 9 January 1997 4 9 3 Liquid Tank temperature The actual liquid temperature in the tank will affect the settling rate The liquid temperature can be changed initially by the instructor but will be dynamically updated based on heat balance with the following relevant factors included Mass of the liquid Specific heat of the liquid Sea water temperature Temperature in levels in the adjacent tanks Shipis speed 4 9 4 Modelling of Residues When the crude oil has been stored in the cargo tanks for a certain period of time deposits of residues will be the result Three types of residues have been modelled hard residues soft residues and drip residues The formation and distribution of residues will be dependent on the state of operation Carrying Crude Oil in the Tank Soft residue Hard residue gradually over time Carrying Ballast Water in the Tank Soft residue Hard residue gradually over time Soft residue
203. onn ktonn L 16 0 L 18 0 L 20 0 L 18 0 L 16 0 L 16 0 L 18 0 L 22 0 L 18 0 L 14 0 L 12 0 L 300 0 L 350 0 L 500 0 L 700 0 L 700 0 L 700 0 L 700 0 L 700 0 L 500 0 L 200 0 L 200 0 H 1 0 H 16 0 H 18 0 H 20 0 H 18 0 H 16 0 H 16 0 H 18 0 H 22 0 H 18 0 H 14 0 H 12 0 CHT2000 VLCC II ws Alarm List H 300 0 H 350 0 H 500 0 H 700 0 H 700 0 H 700 0 H 700 0 H 700 0 H 500 0 H 200 0 BENDING MOMENT section 1 BENDING MOMENT section 2 BENDING MOMENT section 3 BENDING MOMENT section 4 BENDING MOMENT section 5 BENDING MOMENT section 6 BENDING MOMENT section 7 BENDING MOMENT section 8 BENDING MOMENT section 9 BENDING MOMENT section 10 H 200 0 HULL DAMAGE caused by overload SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE SHEAR FORCE section 1 section 2 section 3 section 4 section 5 section 6 section 7 section 8 section 9 section 10 section 11 BENDING MOMENT section 11 Doc no SO 0604 A January 6 1997 2 13 Page 1500 AG15 LM HULL BENDING MOMENTS 1 2 A 006421 ktonm L 300 0 H 300 0 BENDING MOMENT section 1 LM 006422 L 350 0 350 0 BENDING MOMENT section 2 LM D 006423 ktonm L 500 0 Hz500 0 BENDING MOMENT section 3 LM E 006424 k
204. or ventilation purposes the system can be used by opening ventilation valves from deck This will automatically shut off the fluegas suction valves in order to avoid mix CHT2000 VLCC II ws User s Manual Page 4 65 Doc no SO 0603 A 9 January 1997 4 5 25 Inert Gas Distribution 01 41 14 Picture Alarm Running HD 210 Inert Gas Distribution Group 5 1 OR ore ork ore ek 1 I Q l Q I 28 x 1 69 08 8889 16 l 60 98 60 90 6738 13 l ae SS Sl Sate ss sss S Lula Z m omes Eo 2 125 lt 124 123 lt 122 1 1 1 1 1 1 ballast gt 68 09 8832 11 60 08 1 60 08 G724 94 1 1 x 1 1 x 108 1 1 1 1 1 1 P 1 1 1 1 1 Cre ork Ory i orth is 1 1 1 135 134 133 122 131 CHT2000 ULCC II REV 1 1 Each cargo tank is via branch lines and isolating valves connected to the main inert gas line The oxygen content in the inert gas is dependent on the boiler load and the boiler combustion control The mixing process between the hydrocarbon gas content in the tank and the incoming inert gas flow is modelled giving the average content of oxygen and hydrocarbons in the tank at
205. ore to aft m3 h TRANSFER FLOW to aft m3 h MAIN ENGINE FUEL OIL CONSUMPTION m3 h STEAM BOILER FUEL OIL CONSUMPTION knots SHIP SPEED 90 FORE HFO TANK VOLUME tonn FORE HFO TANK MASS m FORE HFO TANK SOUNDING m FORE HFO TANK ULLAGE AFT HFO TANK VOLUME tonn AFT HFO TANK MASS m AFT HFO TANK SOUNDING m AFT HFO TANK ULLAGE CHT2000 VLCC II ws Variable List Page 29 Doc no SO 0604 A January 6 1997 2 55 Page 0074 M MISCELLANEOUS TANKS A B V04130 HFO SETTLING TANK VOLUME C V04131 HFO SERVICE TANK VOLUME D V04132 DO STORAGE TANK VOLUME E V04133 DO SETTLING TANK VOLUME F V04134 DO SERVICE TANK VOLUME 0 04135 96 FRESH WATER TANK VOLUME H I M04140 tonn HFO SETTLING TANK MASS J M04141 tonn SERVICE TANK MASS M04142 tonn DO STORAGE TANK MASS L M04143 tonn DO SETTLING TANK MASS M04144 tonn DO SERVICE TANK MASS N M04145 tonn FRESH WATER TANK MASS O P Q R S T 2 56 Page 0080 M STEAM BOILER MAIN VARIABLES RO3514 0 1 BOILER START COMMAND 703515 lt 0 2 gt STATE 0 1 2 off on up down C D P03500 bar DRUM STEAM PRESSURE E P03501 bar SUPERHEATED STEAM PRESSURE F T03502 degC SUPERHEATED STEAM TEMP G H 603506 m3 h BOILER STEAM FLOW I 003503 m3 h BOILER OIL FLOW J X03504 96 BOILER FLUE GAS OXYGEN CONTENT 703505 BOILER EFFICIENCY L V03523 96 FO CONTROL VALVE POS N O 003507 m3 h STEAM FLOW PUMPS
206. ory is referred to by time NOTE As soon a new Initial Condition is loaded all snapshots are deleted However a snapshot can be stored as an Init Condition has to be done before loading a new initial condition CHT2000 VLCC II ws User s Manual Page 5 12 5 2 1 10 5 2 1 11 5 2 1 12 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Evaluation Editor For evaluation of the student throughout the exercise taking place Input of specified measuring variables under tag name Specify upper and lower limits Will evaluate how the process is maintained by the student during the simulation Evaluation criteria is whether student is able to maintain process within specified limits Running Starts simulation after having frozen the simulation The time starts running and the student s can proceed the exercise When the RUNNING button is pressed a message will inform that the simulation has started Freeze Freezes simulation during breaks or when situation needs time out for evaluation When FREEZE button is pushed a message will inform that simulation is halted The simulator must be in FREEZE before loading an Initial Condition or a Scenario Page 5 13 5 2 1 13 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Ends simulation after a message Pressing STOP and typing yes after prompt will log out of simulator completely and workstation will return to NORCONTROL login window Stop
207. ose 10096 The pump flow and the pump pressure are controlled by the pump speed setting and the discharge valve setting Page 5 35 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 High bearing temperature Running the pump at substantial speed against high discharge pressure may cause a high bearing temperature after a period of time even if the discharge valve is equipped with a recirculating release valve The performance of the pump turbine is dependent on the steam supply pressure and temperature as well as the condenser vacuum These parameters will vary with the pump turbine load Cavitation If the suction head is too low the pump will start cavitating The critical suction head for cavitation will depend on the vaporising pressure of the liquid to be pumped and the current NPSH Net Positive Suction Head of the pump Cavitation will occur on the cargo pumps but is not modelled on the ballast pump Page 5 36 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 This page is intentionally left blank Page 5 37 Doc no SO 0603 A 16 03 00 61 42 49 Picture Alarm Crude Oil Pump 1 Separator TURBINE PUMP VACUUM SEP To Slop Efficiency 2218 92 kMh ka Power E2184 2 kW Level L4 66 69 99 Tora Shaft 095 91 Efficiency 264 659 x Gas pres P1 65 bar F Cav Index 28 08 x Oil conc x 100 00 Vac P 1 Shaft speed N 1966 6 Inlet liqui
208. ose the blower suction and discharge valves Close the flue gas isolating valve Keep full water supply on the scrubber for a minimum of 1 hour Ensure that the water supply to the deck water seal is satisfactory Open line venting valves and ventilate non hazardous area Inert Vent The operator can choose inerting or air venting by either clicking the Inert Gas suction valves or the air suction valves NOTE Before commencing ventilation by fresh air the tanks must be measured for hydro carbon gas concentration If the readings indicate gas concentration above 2 by volume the tanks are to be purged with Inert Gas until the hydrocarbon gas concentration has decreased to less than 2 by volume This will ensure that the atmosphere is kept below the lower flammable limit throughout the ventilation process Inert Press O 2 content Page 5 95 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The Main Line Inert Gas Pressure and the Main Line Oxygen Content is controlled by automatic valves The IG main control valve is controlled by an O2 analyser which will shut of the valve and open the control valve to funnel if the O2 content exceeds 5 If the valve closes due to high O2 content it will have to be manually opened when the O2 content is brought down under 5 The IG pressure control valve will automatically regulate the flow to deck in order to keep the pressure at the selected setpoint when in
209. p of cargo operations CHT2000 VLCC II ws User s Manual Page 4 55 4 5 15 Doc no SO 0603 A 9 January 1997 Ballast Line 00 32 31 Picture Alarm Running 115 Ballast Line Group ONTRO 118 P0 00 Y Ge 00 469 00 468 00 468 00 468 06 468 09 WTSP CT4 WT5S WT2P CT2 WT2S ch ch 24 129 01 37 125 U3 28 08 598 127 08 52 123 01 67 1 2 188 110 wrap 160 00 A 166 06 A H tank top H tank top 7 1 68 08 8784 68 pa H 86 01 p lt 1 85 d 8 68 08 86 68 08 8 05 rs f 8 9 215 x 199 8 1 G 784 7 DE EN i5 x 182 Cargo tank top Survey 1 8284 69 1 1 60 00 A M CHT2000 ULCC II REV 1 3 The ballast line is from the pump room connected into the segregated ballast tanks WT 3 P amp S A separate ballast deck line is fitted for ballasting CT 2 4 and WT 2 5 P S via drop lines CHT2000 VLCC II ws User s Manual Page 4 56 Doc no SO 0603 A 9 January 1997 4 5 16 Slop Tanks and Oil Discharge Monitor 01 31 20 Picture
210. ponents as well as an efficient simulated presentation of a total plant KONGSBERG NORCONTROL Systems CHT2000 includes a comprehensive instructor communication link that allow him to Pre program and store situations Develop and test new training programs Change operational and ambient conditions Freeze current situations for discussions and clarifications with the trainees Setting of single faults or automatic sequential fault The CHT2000 has a layout and instrumentation typical to that of a modern vessel CHT2000 VLCC II ws User s Manual Page 1 3 Doc no SO 0603 A 9 January 1997 1 3 Simulator Configuration The CHT2000 Simulator is implemented on a network of UNIX workstations with an Instructor Station used as a common server The network is an Ethernet protocol UDP IP and the server is equipped with a hard disk storage of 1 0 Gb Data Tape Station is provided for taking back up of the System Software Student Workstations Instructor Instructor Station Station Figure 1 1 Computer Configuration CHT2000 VLCC II ws User s Manual Page 1 4 Doc no SO 0603 A 9 January 1997 1 4 Simulator Concept The OTISS EMULA environment is very flexible The mathematical models and the man machine interface are run as separate programs The communication between them is established by UNIX sockets The program running the mathematical models of the simulated process is called OTISS The Man Machine
211. pply Pressure has to be available to the pump before it is started Speed Setting The speed setting of the stripping Pump governor is set by the instructor The speed control valve will then vary according to the steam supply pressure the back pressure and the flow Small Diameter Line The stripping Pump delivers normally to the Small Diameter Stripping Line but can be connected to the slop tanks The Eductor The eductor works on the principle that the total sum of energy in a liquid flow is constant Bernoulli s law When the liquid flows from A to B and when it is constricted in C a higher velocity is gained in this point The kinetic energy will then increase in this point too Because of the fact that the total sum of energy is constant the static energy is reduced accordingly yelding a lower static pressure in this point This will create a suction if a pipeline is connected The principle is shown in the figure below The suction flow to the eductor is dependent on the suction head the driving flow and the back pressure The eductor delivers always the driving fluid and the suction fluid to the port slop tank The Deck Line Venting Cocks The deck line venting cocks are opened and closed from the deck These cocks have to be open to get the deck lines properly drained The Stripping valves Separate stripping valves are located in the tanks These valves are located closer to the bottom and closer to the
212. prevention of cavitation and overspeed including Speed Surge Control and Flow Surge Control are available Page 5 39 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Speed Surge Control The Speed Surge Control can be handled by means of clicking the AUTO or MANUAL selection In this way the pump speed setpoint is limited automatically by the liquid level If the level is reduced the pump speed set point is reduced accordingly over riding the manual speed setting By clicking on the speed control section button a pop up window with a pen recorder can be viewed This will give information about the operation performance of the controller Flow Surge Control The Flow Surge Control mode can be handled by means of clicking the section In this way the discharge valve opening is limited automatically by the pump suction pressure drop the discharge valve opening is reduced accordingly and will override the manual speed setting The speed Surge Control and the Flow Surge Control can be set simultaneously Tripping If critical conditions occur the pump will be tripped 1 the pump turbine steam supply valve will automatically close The pump will consequently lose power and eventually stop Reset trip Page 5 40 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The pump trip is indicated by a flashing light on the pump control section Before pump can be re started the trip must be reset
213. quid level in the separator tanks The status of the vacuum pump is shown by a lit symbol The system provides automatic throttle control of the COPs in such a way that the cargo tanks are emptied without use of conventional stripping pumps A butterfly valve in the pressure line of the cargo pumps controls pump throughput to follow varying suction demands as oil level falls in the cargo tanks Entrained and occluded gases entering the suction line are separated out before the liquid reaches the pump inlet Air and gas are separated off in the separator tank and pass through its upper section Condensate from evacuated gas is separated off in the seal water tank while vapour is transferred to the sloptanks However if the liquid level in oil gas separator becomes too low gas or air can enter into the pump and cause a lost pumping capability with pump overspeed and cavitation This will be the case if the vacuum pump does not start automatically at low level It can be demonstrated by setting the vacuum pump in manual Page 5 82 5 7 9 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 For training purposes the pump speed and the discharge valve opening can be controlled separately However modern cargo control techniques for prevention of cavitation and overspeed is available This includes Speed Surge Control and Flow Surge Control Line Stripping On completion of discharge all cargo lines and pumps are to be
214. r Rov cn le P00326 X00327 X00330 700353 2 76 V00336 00337 00364 Ar Q m V00361 L V00362 M V00363 Page 40 Doc no SO 0604 A January 6 1997 Page 0120 M CARGO TANK WT 1 P MAIN VARIABLES m m3 h m3 h bar degC L 0 5 25 0 L 0 1 0 1 L 0 0 H 8 0 L 40 0 H 100 0 WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP WTIP TANK ULLAGE measured SOUNDING even keel TANK ULLAGE even keel TANK VOLUME cap 12554 m3 TOTAL TANK MASS incl residues TOTAL RESIDUES IN TANK TOTAL BOTTOM OUTLET FLOW TANK CLEANING SWW or COW FLOW TANK ATMOSPHERIC PRESSURE OXYGEN CONTENT HYDRO CARBON CONTENT CARGO TEMPERATURE Page 0121 M CARGO TANK WT 1 P VALVES lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt lt 0 1 gt WTIP WTIP WTIP WTIP WTIP WTIP BOTTOM VALVE CNTR BOTTOM VALVE STBD COW SUPPLY VALVE INERT GAS SUPPLY VALVE INERT GAS OUTLET VALVE P V bypass INERT GAS P V VALVE CHT2000 VLCC II ws Variable List 2 77 gt 000341 000342 000317 000343 000344 600333 000334 lt 000370 2 78 000310 L00311 L00313 L00314 X00316 M00303 V00302 M00322 M00323 M00324 M00325 M00307 M00306 M00315 D00320 D00321 Q Z O 2 O Z lt i R r Q i 9 Q Z gt CHT20
215. r s Manual Doc no SO 0603 A 9 January 1997 3 INSTALLATION 3 1 Introduction The purpose of this chapter is to provide facility guide lines for installation of the simulator Consistent and reliable performance of the system is dependent on a proper environment including power conditioning air flow cooling and humidity control as well as installation of the system in conformance to standards Achievement of these standards is mandatory for reliable operation and continued compliance with these standards is the basis for warranted performance Specific requirements are provided for the computer and subsystems These requirements are derived from several sources including manufacturers technical documentation standard commercial practices national and local building codes and regulation and most importantly our experience in designing constructing and operating simulator facilities Additional information is included below as recommended guide lines for the system This information is based on experience gained from major simulator installations 3 2 Storage Requirements The simulator equipment may be stored by the customer for a period up to 4 months The following requirements has to be followed Temperature 0 C to 50 C Maximum Temperature Gradient 15 C per hour Relatively Humidity 5 to 90 condensation The equipment must be kept in its original packing unopened The crates must not be stored on top of ea
216. realistic environment To get a true impression of how to run cargo plant the disturbing noise is essential therefore KONGSBERG NORCONTROL has designed a unique synthesised audio system Pump sounds are synchronised with the rpm of the cargo pumps and in addition the noises from diesel engines generators compressors etc are presented by separate sound amplifiers CHT2000 VLCC II ws User s Manual Page 1 2 Doc no SO 0603 A 9 January 1997 1 2 System Description As pioneers in the ship automation field KONGSBERG NORCONTROL Systems a s know how modern technology has improved safety reliability and economy on board ship The improvement has been immense but it is also known that it is impossible to replace the proficiency and know how to an experienced engineer the man who must be present in the right place at the right time to do things quickly and efficiently KONGSBERG NORCONTROL Systems has designed dynamic real time computerised simulator which can compress years of experience into a few weeks and provides hands on training The simulator provides the necessary information on dynamic and interactive processes as found in a real cargo plant The CHT2000 VLCC II ws is designed to meet the demands for basic operational training of junior officers fault studies with economy and optimisation s studies with the senior officers It enables the simulation of individual auxiliary systems sub system and independent com
217. rred to the slop tanks Page 5 77 Doc no SO 0603 A 16 03 00 Ruming Stripping Pump Eductor 1 4 68 08 116 00 61141 9 15 31 DI Gi682 8 gt Eductor Slop 63964 tank X1880 08 PORT 1 81461 9 Stripping Pump 1 88 08 P9 71 60 08 ni Small Diam 198 S shaft speed P0 33 1 65 Line NB 68 spm Speed 4200 0 x 100 00 x 100 00 Ctr d I 68 09 86 1468 line line 4 Ku aS SS seer line line 4 gt lt 68 09 68 08 line 3 line 3 line ees line 3 V 68 08 68 98 line 2 line 2 es line 2 line 2 208 line 1 line 1 68 08 50 08 68 08 11 1 5 SWW COW X over Crude line oil line 168 98 CHT2888 ULCC II REV 1 3 CHT2000 VLCC II ws User s Manual Page 5 78 5 7 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Stripping can be carried by using Stripping The stripping pump The eductor The vacuum strip During stripping operations the main suction valves should preferably be shut while the throttled stripping valves should be kept open The main valves are located higher in the tanks than the stripping valves and not so close to the bulkheads either i e By using the stripping valves instead of the main valves during the stripping procedure influx of air inert gas into the
218. rt and the starboard slop tank The Clean Water Interface Level Port Slop Tank must be higher than the Decanting Line Outlet Height Port When filling the port slop tank the clean water will be forced into the slop decanting line to prevent the entrance from clogging oil and dirt in the line Separation in the Port Slop Tank After some time the mixture of oil and water will separate Page 5 88 5 7 14 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Decanting the Port Slop Tank Check that appropriate fluid separation has taken place Check Clean Oil Interface Level Check Clean Water Interface Level Check that the level in the port slop tank is substantially higher than the level in the starboard tank Open the Interconnecting Valve in the Slop Decanting Line A gravity flow between the port and starboard slop tank will start Check continuously to ensure that clean water is flooding the suction piece of the slop decanting line Check also to discover if any significant traces of oil are present im the slop decanting line If one of these events occurs or as soon as the port and starboard slop tank levels have been equalised the Slop Decanting Line Valve should be closed immediately Page 5 89 5 7 15 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Oil Discharge Monitor The starboard slop tank can be emptied through the Overboard Line The following procedure can
219. ry out economical studies of the cargo handling operation thus improving cargo handling efficiency Pollution Control The simulator has an oil monitoring system which continuously measures all liquid pumped overboard A preset limit for acceptable oil in the overboard liquid can be set by the operator assuring that no polluted liquid will be pumped overboard The computer will accumulate the amount of oil pumped overboard and calculate the amount per nautical mile Time Scale Time factor is in Normal operating mode set to time factor Real time From picture no 1000 Operating condition the dynamic response time can be selected In Fast mode the dynamic response time will have time factor 5 and in Very fast mode the factor will be 20 Period The simulation period will be the result of actual simulation time multiplied by the time factor from when the operating mode was selected Ship state The ship speed can be set from the Variable page 0003 Sea Ship state During loading discharging operations this should be set to zero The speed will have effect on the HFO consumption the trim the cargo temperature and the ODM when in use Weather condition The weather condition is selected from the Variable page 0003 Sea Ship state Condition is selected by entering wind force 0 12 after the beaufort scale The weather condition will have influence on HFO consumption trim and heel rolling shear forces deflection
220. s The normal cycle of tanker operation comprises loading laden voyage discharging ballasting ballast voyage tank cleaning ballast shifting and reloading Loading is accomplished by following directions given in the ship s loading orders Discharging is accomplished by discharging the cargo directly into a terminal tank storage area or into a tank barge for further transport During the discharging procedure the vessel may also effect the COW procedure Ballasting is a process whereby sea water is taken aboard into the cargo tanks or into segregated ballast tanks to ensure proper propeller immersion and to provide good manoeuvring and sea keeping characteristics Page 5 1 5 1 5 1 1 5 1 2 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 TEC2000 Graphic Workstation The following pages will describe operation of the tracker ball the HP keyboard the Instructor the Alarm and the Operator sections Tracker ball Connected to the TEC2000 functional keyboard there is a tracker ball comprising a roller ball and 3 buttons The roller ball moves the cursor on the screen Function of left button is START pump compressor or open valve The middle button the select button utilises operation of buttons in the model drawings retrieval of new sub systems or call display windows The push button on the right hand side is used for execution of commands to STOP pumps compressors CLOSE valves or reset of malf
221. s to be created in the same way as malfunction editor Input of tag names similar to malfunctions editor adding underscore S after the Malfunction tag When starting a scenario malfunctions and actions which are activated during the simulation must be chosen by clicking on software buttons Changing colours will indicate which buttons are activated In front of each button there is a light with 2 circles Outer circle lit means action is activated but waiting for set time interval to be reached in order to switch action on Inner circle lit means that READING is active meaning set intervals are reached and action started On the bottom half of screen buttons A41 to 80 is event malfunctions Used and created as malfunction but triggering actions instead of malfunctions Such as closing of valves Sound Toggles sound system on off Valid for operational trainer only Page 5 11 Doc no SO 0603 A 16 03 00 5 2 1 7 Time Editor Allows altering the time for which the malfunctions or actions to take place Clicking on CHANGE TIMEPHASE software button enters a line on time section of picture Use the inner scroll buttons to increase or decrease the time between actions or events to take place Outer scroll buttons to changes time phase 5 2 1 8 Event Editor Used to supervise and allows adjusting events and event conditions 5 2 1 9 Snapshot Takes a snapshot of simulation for later reference Places snapshot in snapshot direct
222. ss where by sea water is loaded into the cargo tanks into segregated ballast tanks to ensure proper immersion and to provide good manoeuvring and stability characteristics In order to lessen hull immersion and thus reduce fuel consumption minimum quantities of ballast should be taken However the quantity must be sufficient to submerge the propeller maintain vessel manoeuvrability to avoid excessive vibration to operate within approved stress limits and to retain sufficient bow immersion Ballasting Ballast should be evenly distributed to minimise stress Tanks should be either empty or full Partially full or slack tanks should be avoided An appropriate stern trim will enhance propulsion efficiency An optimum trim for the CHT 2000 VLCC II ws vessel is about 4 5 meters 15 feet Ballasting include handling three types of ballast Segregated ballast Dirty ballast departure ballast Clean ballast arrival ballast Page 5 69 5 7 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Ballast Pump Ready The ballast pump is ready for start up if the mimic section is lit Trip The TRIP symbol is lit if one or more of the following condition are present Steam supply pressure is too low Condenser pressure is high These conditions can be set by the engineers i e the instructor Starting Procedure The pump is started by clicking the START symbol The following is normal start procedure
223. ssure can be caused by leakage from tank openings or by falling air and sea temperatures Inerting during Discharging Cargo discharge shall not be started until All cargo tanks including slop tanks are connected to the Inert Gas main All Inert Gas tank valves are locked open All other cargo tank and slop tank openings including P V by pass are closed The Inert Gas plant is operating producing Inert Gas with an O content of no more than 5 90 Inert Gas purging prior to Gas Freeing When it is necessary to render a tank gas free after washing the concentration of hydrocarbon vapour must be reduced by purging the inerted cargo tank with Inert Gas until the hydrocarbon content of the tank atmosphere has been reduced to 2 by volume Page 5 65 5 6 9 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 must be taken to ensure that testing is representative of the entire tank atmosphere Gas Freeing Gas freeing of cargo tanks is only to be carried out when tank entry is essential Gas freeing is not to be started until the hydrocarbon gases have been purged from the tank to a dilution of 2 or less The tank being gas freed is to be positively isolated from Inert Gas deck main line and from other tanks Gas freeing is to continue until the entire tank has an O content of 21 by volume and a reading of less than 1 90 of the lower flammable limit L E L is obtained Care must be taken to prevent t
224. ssure in all cargo tanks When cargo tanks are gas free on arrival at the loading port the tanks are to be inerted before they are loaded Purge cargo tanks with Inert Gas to make the transition from Cargo vapour condition to gas free condition without passing through the explosive limits In order to maintain cargo tanks in a non flammable condition the Inert Gas plant will be operated to Inert empty cargo tanks Supply positive pressure during cargo discharge deballasting and as necessary in other tank operations Top up pressure in the cargo tanks when necessary during the voyage Page 5 62 5 6 3 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inerting Empty Tanks When inerting empty tanks which are gas free following a dry docking or tank entry Inert Gas should be introduced through the distribution system while the air in the tank is vented into the atmosphere via the P V by pass Inerting should continue until all the tanks have an O content of less than 8 by volume Tanks with wash bulkhead may provide pockets of high O content These tanks should be doubled checked The process can be monitored from the respective Tank Atmosphere Pictures MD 222 235 On the completion of inerting all tanks should be consistently pressured and with Inert Gas A positive pressure of at least 0 1 Bar can be maintained by topping up with Inert Gas as necessary Loading must not be started un
225. t 1 gt Ullage meter slop U1 85 A U6 68 A 125 28 MEN 08 43 01 12 A U6 52 WT 6 P MT SP HT 4 P WT 3 P HT 2 P HT 1 P 138 129 128 115 127 126 CENTER Ullage meter HFO CT 4 2 HFO FPT 261 125 124 123 122 261 115 STARBOARD lt 1 gt 025 28 11 67 Ullage meter MT 65 MT 5 WT 4 3 5 MT 2 S HT 15 135 134 133 115 122 131 DEADWEIGHT 180 80 1000 ton 96 17 7 of summer mark CHT2000 ULCC II REU 1 2 Doc no SO 0603 A 16 03 00 5 4 3 The Loading Plan The loading plan should show the following details Names and quantities of the products to be loaded Cargo breakdown The pipeline system to be used for each grade The sequence in which products are to be loaded and discharged The final ullage Forward amidships and aft sailing draft Identification of all cross over and sea valves to be closed and or sealed Required loading rate CHT2000 VLCC II ws User s Manual Page 5 45 Doc no SO 0603 A 16 03 00 00 17 38 Picture Alarm Cargo Deck Line 187 Venting valves V 166 00 Deck line x 166 08 Deck line 166 06 G4777 1 Deck line 166 66 64753 Deck line 1 P6 04 gt x 100 00 08 08 68 08 08 89 08 08 2 V 1 CHT2000 ULCC II REU 1 1 CHT2000 VLCC II ws User s Manual Page 5 46 5 4 4
226. t does not support combustion No oil burner is 100 perfect It is therefore necessary to add more than the theoretical needed amount of air and this result in an excess of O and CO content in fluegas as a result of incomplete combustion Not all of the oxygen in the air will be combusted and some fuel will not get sufficient oxygen for complete combustion Therefore some carbon monoxide CO will remain The sulphur dioxide SO comes from the sulphur content in the fuel and the water vapour comes from the combustion of the fuel hydrogen compounds 1 kg fuel oil combusted in the boiler with normal excess of air gives approximately 12 m Inert Gas after passing the scrubber cooling tower Under normal service conditions of the boiler for this particular ship the fuel oil consumption is about 6 000 kg h The capacity of the Inert Gas plant is 40 000 m3 h which means that approximately 50 96 of the total amount of flue gas passes through the Inert Gas plant To comply with IMO Rules the O content is not to exceed 5 in the Inert Gas main supply line or 8 in cargo tanks Page 5 61 5 6 2 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inert Gas Policy All cargo tanks to be inerted at all times except when entering is necessary Cargo tanks are to be kept in inerted condition whenever they contain cargo residues or ballast The oxygen content is to be kept at 8 or less by volume with a positive gas pre
227. t into the port slop tank via the eductor Start the driving pump and adjust to deliver the required driving pressure The pressure of the driving medium should be set according to the level in the port slop tank As soon as the driving pump delivers with normal working pressure the suction valve s can be opened The suction valve s are not to be opened until the required pressure has been obtained because if the pressure is lower than approx 3 0 bar the driving medium may run in the wrong direction and fill the tanks instead of emptying them Before stopping the driving pump the suction valve s should be closed to prevent water oil from entering the cargo compartments The eductor is installed to eliminate use of the stripping pump during tank cleaning If the eductor is used for COW or stripping of cargo the eductor must be driven with the same type of driving medium as the cargo to be stripped out In order to avoid filling up the slop tank too quickly the driving medium should be taken from the slop tank Page 5 81 5 7 8 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 The drawback of using the eductor for cargo stripping is that the stripping puts liquid into the port slop tank which later has to be discharged ashore by means of an ordinary pump The Vacuum Strip Oil Gas Separator The cargo pumps are furnished with oil gas separators with vacuum pumps The vacuum pumps are started automatically at low li
228. t tanks The system consist of 4 main cargo lines and 1 separate ballast line all located in the centre tanks The main cargo lines are interconnected via cross over lines and isolating valves Cargo and ballast tanks are connected to the main lines via branch pipes and isolating valves Main and stripping suctions bell mouths are located in aft end of the tanks and relatively close to the longitudinal bulkheads in order to obtain maximum out turn during discharging stripping and COW ing CHT2000 VLCC II ws User s Manual Page 4 53 Doc no SO 0603 A 9 January 1997 4 5 11 Cargo Line 1 00 30 23 Picture Alarm Running MD 111 Line 1 Group 108 DECK LINE 1 Line venting 112 G 4 14 EE p to deck line 2 Y 64761 6 P6 97 P6 63 100 00 x 188 00 1 88 00 199 119 WTSP 1 129 iT 1 68 08 1 68 08 1 68 08 1 88 40 4 04 0 COP 1 Vac 4 81508 5 4 81893 0 Sep P 10 20 A GU761 u 64751 3 P1 70 Pt P 1 87 lt x 100 00 x 100 00 Enea 1 55 6 211 P1 99 58 P 8 78 x 100 00 x 100 08 x80 00 x 100 00 1 68 09 Crude oil Slop SHH COM S H suct suct X over X over X over X over line line line line 189 199 199 189 to bot line
229. tance between the centre and gravity G and the vertical line through the new centre of buoyancy B is denoted GZ and represents the arm of the rectifying moment At small angle of heeling which normally will be the case GZ 8 9 The total rectifying moment counteracting the heeling will then be p gVp GM 510 Thus When GM gt 0 gt gt 0 I e The heel will be counteracted and the ship is said to be stabilised WhenGM 0 gt 0 The heel will remain and ship is said to be indifference WhenGM lt 0 gt lt 0 I e The heel will increase and the skip will be unstable The considerations above are based on the height GM which is called the Meta Centre Height GM KB KG ref fig Ship Heeling GM KB BM KG GM KB I Vp KG Where I The waterplane s longitudinal moment of inertia at the actual draught VD The volume displacement at the actual draught I CILBT3 Then CHT2000 VLCC II ws User s Manual H Page 4 34 Doc no SO 0603 A 9 January 1997 GM T KG CHT2000 VLCC II ws User s Manual Page 4 35 Doc no SO 0603 A 9 January 1997 Load distribution The relationship between the load distribution the shear force the bending moment and the deflection can preferably be illustrated by considering a straight beam with an even load q0 The relationship between the load distribution and the shear force the bending moment and
230. tank valves must be checked to ensure that those valves which should be closed actually are closed Page 5 47 Doc no SO 0603 A 16 03 00 90 16 26 Picture Rlarm Running HD 10 Load i Discharge Group LOADING LOAD DISCHARGE DISCHARGING Temp 68 08 deg C Density 0828 08 kg m3 Connected Connected to manifold 4 3 2 1 to manifold 4 3 2 1 Pressure P5 89 bar Pressure P2 94 bar Drop Const P0 98 bar Rise Const P4 90 bar 108 6 4771 P6 03 x 100 00 100 00 100 00 100 00 118 CHT2000 VLCC II ws User s Manual CHT2000 ULCC II 1 2 Page 5 48 5 4 6 5 4 7 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Setting P V valves The vessel should use closed loading which means loading with closed ullage sounding and sighting ports except for initial and final inspection Vapour displaced by incoming cargo should be vented via the P V valves which will ensure that vapour are taken clear of the cargo deck Ensure that the Inert Gas plant is shut down the deck isolating valve is shut and that the main Inert Gas venting valves are open Manifold Valve s The manifold valve s shall remain shut until the vessel is completely ready to load and not opened until confirmed from the Terminal Page 5 49 Doc no SO 0603 A 16 03 00 5 4 8 Commencement of Loading When all necessary valves in the loading system are checked open and the vessel has signified its readiness load
231. til the vessel s cargo tanks are fully inerted Page 5 63 5 6 4 5 6 5 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inerting during Deballasting Deballasting from cargo tanks should not start until All cargo tanks including slop tanks are connected to the Inert Gas main All Inert Gas tank isolating valves are locked open All other cargo tank and slop tank openings including P V by pass are closed The Inert Gas plant is producing Inert Gas with O content of 5 or less When loading and deballasting concurrently pressures throughout the Inert Gas system must be carefully monitored Inerting during COW and Water Washing Before each tank is washed the O content is not to exceed 8 by volume The content and Inert Gas pressure must be continuously recorded during the washing operation If the O content exceeds 8 or the tank atmosphere is no longer positive the washing operation must be stopped until satisfactory conditions are restored Page 5 64 5 6 6 5 6 7 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Inerting during Loading When loading cargo the Inert Gas main deck isolating valve is to be closed and the inert gas plant shut down unless other cargo tanks are being deballasted simultaneously The Inert Gas deck branch valves must be locked in open position During the loaded voyage a positive pressure of at least 0 1 Bar must be maintained Loss of pre
232. tion the fixed values will remain the same The fixed process is valid for the following systems Page 5 6 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Boiler Boiler isolation sets the steam pressure to cargo pumps at 15 bar Boiler fluegas oxygen content to 3 5 Inhibit The demand for realism with regard to what kind of alarm indication to be most appropriate depends on the training situation and the number of students present The functions are disabled when pressed For the maximum version the following functions are available Alarm Horn and alarm lamp operational only Keyboard Buzzer internal in the TEC2000 panel Page 5 7 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Process Dynamics Changes the simulator time response of the different sub systems The faster response the shorter time is required to establish normal temperatures in tanks correct viscosity etc There are 3 choices Normal Fast Very Fast Log printer 1 Determines which events or alarms to be logged on the printer If required all buttons can be activated Press the appropriate push button s to satisfy the exercise to be run The actual event alarm is printed together with the time it took place The choice is as follows Alarm In general all alarms that occur are printed Event All actions from the student are printed like start stop of pumps opening or closing valves DataChief All actions from t
233. tions in connection with low suction head Running Increase Decrease The set point of the pump turbine governor which regulates the pump speed is controlled by enter a new value into the controller Open Close The discharge valve setting is controlled by means of a new value CHT2000 VLCC II ws User s Manual Page 4 67 Doc no SO 0603 A 9 January 1997 The pump flow and the pump discharge pressure are controlled by the pump speed setting and the discharge valve setting High Bearing Temp Running of the pump at a substantial speed against a high discharge pressure may cause high bearing temperature after a certain period of time even if the pump is equipped with a recirculation safety valve The performance of the pump turbine depend on the steam supply pressure and temperature as well as the condenser vacuum These parameters will vary with the pump turbine load Cavitation If the suction head is too low the pump will start to cavitate The critical suction head for cavitation will be dependent on the vaporising pressure of the liquid to be pumped and the current NPSH Net Positive Suction Head of the pump This phenomena will occur on the cargo pumps but not on the ballast pump CHT2000 VLCC II ws User s Manual Page 4 68 Doc no SO 0603 A 9 January 1997 4 6 MODELLING OF PUMP CHARACTERISTICS The relationship between discharge head flow and pump speed of a centrifugal type pump can be described as follows
234. to the carriage of clean ballast water only SBT require separate pumps and pipes dedicated to handling ballast water only The modelled SBT are WT 3 P S and FP and ballast can be pumped to from tanks by the ballast pump in the cargo pump room Segregated ballast may be retained on board in order to restrict the air draught if necessary because of weather conditions or restrictions of loading arms or shore gangway However care must be taken not to exceed the maximum draught for the Terminal or for hull stress Page 5 75 5 7 3 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Dirty Ballast Departure Ballast Dirty Ballast is pumped into WT 2 P S and WT 5 P S via the ballast pump and separate ballast drop lines This operation can be performed during discharging and after the tanks have been COW ed Dirty Ballast tanks can be deballasted only by using the cargo pumps and lines It is now common practice to discharge all cargo tanks before ballast is pumped into any cargo tanks This practice is followed in order to avoid claims for short discharging and or ROB Remaining on Board If it is necessary because of draught air draught trim stress to ballast empty cargo tanks while simultaneously discharging other cargo tanks ensure that the following conditions are met A proper line strip is done and tanks are completely drained of cargo These results should be verified by Terminal representative surveyor
235. tonm L 700 0 H 700 0 BENDING MOMENT section 4 LM 006425 ktonm L 700 0 H 700 0 BENDING MOMENT section 5 LM 006426 L 700 0 H 700 0 BENDING MOMENT section 6 LM H Q06427 ktonm L 700 0 H 700 0 BENDING MOMENT section 7 LM I 006430 L 700 0 H 700 0 BENDING MOMENT section 8 LM J 006431 L 500 0 H 500 0 BENDING MOMENT section 9 LM 006432 ktonm L 200 0 H 200 0 BENDING MOMENT section 10 LM L 006433 ktonm L 200 0 H 200 0 BENDING MOMENT section 11 LM M N O P Q R 5 2 14 1501 AG15 LM HULL SHEAR FORCES 2 2 A B 06401 L 16 0 H 16 0 SHEAR FORCE section 1 LM D 06402 L 18 0 H 18 0 SHEAR FORCE section 2 LM E 06403 ktonn L 20 0 H 20 0 SHEAR FORCE section 3 LM F 06404 ktonn L 18 0 H 18 0 SHEAR FORCE section 4 LM P06405 L 16 0 H 16 0 SHEAR FORCE section 5 LM H 06406 L 16 0 H 16 0 SHEAR FORCE section 6 LM I P06407 L 18 0 H 18 0 SHEAR FORCE section 7 LM J 06410 L 22 0 H 22 0 SHEAR FORCE section 8 LM 06411 L 18 0 H 18 0 SHEAR FORCE section 9 LM L 412 ktonn L 14 0 H 14 0 SHEAR FORCE section 10 LM M 06413 L 12 0 H 12 0 SHEAR FORCE section 11 LM AP ANH MVOZ Page 10 CHT2000 VLCC II ws Alarm List 2 15 A B L03534 D 03555 X03556 F G H P03550 I X03552 J
236. uctor or arise by incorrect operation Page 5 33 Doc no SO 0603 A 16 03 00 00 20 01 Picture Alarm Cargo Pump Room 128 Lh 60 00 High Overboard Lh 69 99 116 68 08 Sloptank T optan 4 09 0 pEj E COH 69 88 gt Eductor 2 5 gt P9 71 G4 66 S H 4 168 08 suct S P 68 08 68 00 COP 4 Bot line Bot line 3 SWH COW Ballast line line Bot line 2 P 8 5 20 Bot line 1 V ML suct X over line P9 00 G4777 4 Gu777 3 COP 2 G4767 9 6476 8 P8 94 COP 1 vac sep 100 02 18 08 CHT2000 ULCC II REV 1 2 CHT2000 VLCC II ws User s Manual Page 5 34 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Starting Procedure The pump is started by clicking the start symbol The following is the normal starting procedure for centrifugal type pumps Close the discharging valve Open the suction valve Fill the pump with liquid oil water Start the pump Open the discharging valve Increase Decrease The set point of the pump turbine governor which regulates the pump speed is controlled by the Speed surge controller by selecting the speed control button and enter a new RPM value The discharge valve setting is controlled by means of the Valve control button Select valve position by clicking in the window in the control button and enter an opening value 0 Open Cl
237. ume CBM LCG m VCG m 3 800 263 86 13 41 HFO TK AFT 3 800 48 51 13 96 Cargo Pumps 4 Centrifugal Type Cargo Pumps 4 000 cbm h 120 mLC Oil Gas Separators 4 Gas Oil Separators Stripping Pumps 1 Reciprocating Stripping Pump 350 cbm h Stripping Eductor 1 Stripping Eductor 1500 cbnyh Ballast Pump 1 Centrifugal Type Ballast Pump 4 000 cbm h 120 mLC Cargo Lines 4 segregated cargo lines Size CHT2000 VLCC II ws User s Manual Page 4 2 Doc no SO 0603 A 9 January 1997 Ballast Line 1 segregated ballast line Size P V Valves One for each tank 0 45 0 45 mWC CHT2000 VLCC II ws User s Manual Page 4 3 Doc no SO 0603 A 9 January 1997 4 2 Computer System The graphic workstations are in principle used for running general UNIX applications However UNIX is concealed in the simulator as soon as the operator has logged in The work stations will thereafter be operated in a graphic man machine interface in a point and click fashion by using a dedicated operational keyboard and a roller ball On the operator stations the operator student s can view mimic pages representing the various simulated systems These graphic mimic process diagrams are interactive i e the process can be both monitored and controlled In principle all the graphic workstations can be configured as instructor stations Whenever a workstation is going to be used in part task mode t
238. unctions introduced Keyboard The keyboard is used to change set point of controllers new model drawings change variables in the variable list change intensity of malfunctions A type text strings in connection with creation of scenarios and initial conditions Page 5 2 5 2 5 2 1 5 2 1 1 CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 16 03 00 Operating panels The TEC2000 functional keyboard comprises three panels the Instructor section the Alarm section and the Operator section A brief description in utilising these functions are described in the following pages For further detailed information of the TEC2000 functions please read the TEC2000 Instructor Manual Function buttons at the Instructor section The functions located at this panel are only accessible when in Instructor mode all except the RUNNING FREEZE STOP and SCENARIO which can be selected from Operator Mode Instructor Operator switch selector Chooses between Operator and Instructor mode When the key is in Instructor mode a push on one of the two push buttons next to the key will toggle between Instructor or Operator mode When in Operator mode input from nearly the whole Instructor section is inhibited With regard to the Malfunction lists only the list of malfunctions are visible without any indication of what failure is introduced nor the intensity Page 5 3 5 2 1 2 CHT2000 VLCC II ws User s Manual Doc no S
239. ured R S T CHT2000 VLCC II ws Variable List Page 81 Doc no SO 0604 A January 6 1997 2 159 Page 0510 M TANK COW VALVES A 00164 0 1 CT1 COW SUPPLY VALVE V00264 lt 0 1 gt WTIS COW SUPPLY VALVE C V00364 0 1 WTIP COW SUPPLY VALVE D E V00464 0 1 CT2 COW SUPPLY VALVE V00564 0 1 WT2S COW SUPPLY VALVE V00568 0 1 WT2S COW SUPPLY VALVE H 00664 lt 0 1 gt WT2P COW SUPPLY VALVE I 00668 0 1 WT2P COW SUPPLY VALVE J 1164 lt 0 1 gt CT3 COW SUPPLY VALVE L 01264 lt 0 1 gt WT4S COW SUPPLY VALVE M V01364 lt 0 1 gt WT4P COW SUPPLY VALVE 01464 lt 0 1 gt CT4 COW SUPPLY VALVE 1564 lt 0 1 gt WTSS COW SUPPLY VALVE P 01568 lt 0 1 gt WTSS COW SUPPLY VALVE 01664 0 1 WTSP COW SUPPLY VALVE V01668 0 1 WTSP COW SUPPLY VALVE S 1764 0 1 WT6S COW SUPPLY VALVE T 02064 lt 0 1 gt WT6P COW SUPPLY VALVE 2 160 Page 0512 M P V BYPASS VALVES A 00162 lt 0 1 gt INERT GAS OUTLET VALVE P V bypass V00262 lt 0 1 gt WTIS INERT GAS OUTLET VALVE P V bypass D V00362 lt 0 1 gt WTIP INERT GAS OUTLET VALVE P V bypass E F V00462 lt 0 1 gt CT2 INERT GAS OUTLET VALVE P V bypass 00562 lt 0 1 gt WT2S INERT GAS OUTLET VALVE P V bypass H 00662 lt 0 1 gt WT2P INERT GAS OUTLET VALVE P V bypass I J 1162 lt 0 1 gt CT3 INERT GAS OUTLET VALVE P V bypass K L 0146
240. uring simulation must be chosen by clicking on software buttons Changing colours will indicate which buttons are activated In front of each buttons is a light with 2 circles Inner circle lit means that READING is active meaning set intervals are reached and action started Outer circle lit means action is activated but waiting for set time interval to be reached in order to switch action on Time Editor Allows editing of response time Active only in instructor mode CHT2000 VLCC II ws User s Manual Page 4 18 Doc no SO 0603 A 9 January 1997 INSTRUCTOR 11 INIT COND OPERATION SCENARIO DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE Instructor Clicking on CHANGE TIMEPHASE software button enters a line on time section of picture Using inner scroll buttons to locate change line between actions or events to be changed Then outer scroll buttons to change time phase Event Editor Active in instructor mode only Allows editing of events meaning specific actions or malfunctions to be initiated in proper sequence Snapshot Takes a snapshot of simulation for later reference Places snapshot in snapshot directory with time date reference Active only in instructor mode CHT2000 VLCC II ws User s Manual Page 4 19 Doc no SO 0603 A 9 January 1997 Evaluations Editor For evalu
241. utomatic circuit breakers Voltage 230 AC 15 V AC RMS Single phase Frequency 50 Hz 0 5 Hz Permitted Voltage Fluctuation For duration of 5ms 20 or 10 of normal phase voltage For duration of 30m 15 of normal phase voltage Permitted Amplitude Distortion The momentary voltage may not differ more than 6 from a sinusiod voltage of the same RMS voltage Start Current CHT2000 VLCC II ws User s Manual Page 3 3 Doc no SO 0603 A 9 January 1997 Up to 5 times normal current dependent on the configuration The start current may vary from 10 ms to 10 seconds dependent on the configuration Power Consumption Up to 3 5 kVA is required to run a full scale simulator CHT2000 VLCC II ws User s Manual Page 3 4 Doc no SO 0603 A 9 January 1997 CARGO HANDLING TRAINER CHT2000 VLCC II ws Chapter 4 Functional Description CHT2000 VLCC II ws User s Manual Doc no SO 0603 A 9 January 1997 4 FUNCTIONAL DESCRIPTION 4 1 Introduction The modelling of this Cargo Handling Trainer 2000 is based on the following Vesselis particulars M T Polar Lady Loa Lpp Cargo tanks Net volume CBM LCG m 12121 Segregated Ballast Tanks Net volume CBM LCG m VCG m 12 113 276 19 13 99 WT 3B 5 10 460 165 62 12 63 CHT2000 VLCC II ws User s Manual Page 4 1 Doc no SO 0603 A 9 January 1997 Tanks Net vol
242. will be indicated on pictures right side To create click on software button CREATE and click on one of the buttons M01 to M40 and type in chosen name IMPORTANT When a malfunction name has been typed and ENTERED a prompt will ask you which TAG name is wanted THIS TAG NAME MUST BE WRITTEN WITH FULL STYLE NAME AND NUMBER DIRECTLY COPIED FROM MALFUNCTION LIST IN ADDITION TYPE IN EITHER 5 5 OTHERWISE TAG WILL NOT ENTER WHEN PROMPT CHANGES COLOUR IT WILL BE WRITTEN 0201 S AND YOU ARE ALLOWED TO CONTINUE In section VALUE active and passive values are entered When prompted type in values either digital 0 1 2 etc or analog in percentage of max values CHT2000 VLCC II ws User s Manual Page 4 15 Doc no SO 0603 A 9 January 1997 INSTRUCTOR OPERATOR INIT COND OPERATION DIRECTORY CONDITIONS MALFUNC ACTIONS EDITOR EDITOR TIME EVENTS EDITOR EDITOR SNAPSHOT EVALUATION SNAPSHOT EDITOR REPLAY DIRECTORY RUNNING FREEZE ACTIVE Value entered is value when fault is activated Either one triggered as one continuos fault or as repeating fault PASSIVE Value entered is starting level That is condition of operation before fault is activated UNIT Engineering unit or percentage Not necessary to be entered AUTOMATIC MODE Activating this will make fault go active and stay active when entered time is reached Activating this button will make fault go active and then off aga

Download Pdf Manuals

Related Search

Related Contents

議員提出議案第14号 国による公的森林整備の推進と国有林野事業  Manual do Proprietário  Random Orbital Sander Random Orbital Sander  Télécharger  JALOUSIE - Robert Juliat    ダウンロード  Cooler Master RA-USB-3002-IN  20-23ページ(PDFファイル)  METRA HIT - GMC-I Messtechnik GmbH  

Copyright © All rights reserved. Failed to retrieve file