ー) Thin Ship 理論による造波特性の計算プロ グラム
Contents
1. 2 2 1 2 R Calculation of Optimum Source Distribution by Variational Method for Fore Body 2 2 2 3 48 10 2 4 Cosine2. CAL WRITE 2 2 1 SUBROUTINE DATPRT Date and Time Print 2 2 2 3 51 3 2 4 DATTIMD LP 3 50 B gt CALL DATTIM 1
3. gt 0 hid Green 3
4. Finite Element Method 2 2 1
5. T 2 21 Hydrodynamic Forces Two Dimensional Rectangular Cylinder 2 2 2 3 50 4 2 4 1 100 f o y X 5 gt 1 DD r INS yix y K 454564 2 p S z 7 7 lt 1 1 G Gr iGr 9 9 S7 5 Gr log 2
6. 2 2 1 2 2 2 3 51 10 2 4 i GRAPH 1 READIN 09
7. 3 2 2 1 19 TOSBAC 5600 55KW DI SC 5LINKS 2 2 2 3 49 1 2 4 a 5 n 95 9 0 6 19050 1
8. 1 X ray Attenuation Coefficients From 10 kev to 100 Mev G W Grodstein NBS Circular 583 1957 R T McGinnies Supplements to NBS Cir cular 583 1959 2 Applications of Monte Carlo H Kahn USAEC Report R 1237 1954 29 16 1 1
9. 2 2 1 1 BLO DAC 1V 2 2 KK 2 3 51 1 2 4 BLOPRE BL OPRE 1 MDYCR 1 Moody 2 START 1
10. 1 MC33 2 6 JIS7000 FORTRAN MC33 GCOS 540 2 MC33 GCOS 16kMW TOSBAC 5600 120 10 10 3
11. 3 KOROR 0 HEDA k VAHO O 9 2 5 1 2 6 TOSBAC 5600 30KW
12. 3 S G LT S G a a 4 BE i Blasuis ii Rander Bla suis 33 5 45 90 180923 b b 6 c AL 2 Pr c 7
13. MT C INPUT 2 R B et al Transport Phenomena John Wiley amp Sons Inc 1960 18 1 1 D 1 2 2 1 31 32 NSTOPS 2 2 2 3 49 4 2 4
14. 1 1 DO Re Peit 9 1 0 52 5 2 z 2 7 2 0 Du s 2 y KA 96 5 5 FCKoh 1 cosh 2 2Koh sinh 2K04 A Simpson Green 1 3 yix 2 x x cos ap
15. 17 1 2 2 1 SPP8L 1 Self Pressurizing Process 2 2 80 2 3 50 11 2 4 bulk flow A molar molar
16. CA L BLOCK DATA 2 2 1 Co S SUBROUTINE THRM BLOCK DATA 2 2 2 3 50 4 2 4 BLOCK COMMON 5 298 6000 K 0 2 1 K 298 6000 1 15 2 5 1 2 6 5600 FORTRAN 1008 BLOCK DATA START lt 298 0 0 00
17. 3 9 0 OWN Ka 9 w 2 4 1 6 8 41 2 4 2 ie 6 4 1 8 4 99 2 4 3 HAE V 9 2 2 4 4 4 0 2 5 EPBUCK Cr 140 2 2 6 TOSBAC 5600
18. 4 FOURIE IZAERA RREKO N 9 10 6 1 Lewis form IODE Di richlet
19. 1 26 1975 12 2 gt 0 co 28 1976 12 4 1 2 Volterra Fredholm Bernoulli 2 2 1
20. 2 5 2 6 1 TOSBAC 5600 90kKW 140 TOSBAC 5600 9 50 1 3 4 5678910 gt 43 1 50 1 600 1 150
21. 3 3 1 MT START READ FROMGCARDS starting TEST No Sampting Rate etc READ TEST NO yes READ TIME SERIES WRITE TEST RESULTS DOM FREQ TO L P 8 TEST CALB 8 3 SUBROUTINE FIGURE TEST REFERENCE CH 8 TEST CALIB CONSTS READ FROM CARDS READ FROM FILE TEST NO S TEST yes SUBROUTINE FOURIER 3 2 FIGURE Z
22. 5 2 5 START L CALL RANS12 10 2000 CALL REAA CALL REAC 1 2 6 270 20 TOSBAC 5600 04 10 22K 3 3 1
23. CONVDT SEMLOG SORT 39 40 NY 54 921535 77 9 i lt oN 5441 lt 36 lt BA d 34110904475 01275159 lt 4 9 gt gayaz T 28411044405 1089415 _ Tass 75775 1 wa 814 34 40 41 1 Q VINIT 110044 3 7 4948905 9 RI 5121
24. at T c t 2 4 3 1 1 V amp mg kg 3 Kcal kg 47 48 S Kcal kg K S Kcal kg Cp Poise kg m sec VIC nf sec RM Kcal m hr C 2 2 4 3 2 2 4 2 4 3 3 8 5 Z kg cm2 mkg Kcal kg S Kcal kg K 2 8 1 7 OD G 2 P
25. 5 0 0 2 0 3 sin utun 5 Er log Kr y Z COS 0 7 7 0 577216 Euler S 9 5 sin n 0z 2 2 S 2 g 1 2 3 D z f oo 8 sin 5 00 2 64 2 000 97 cos 45 2 Kx ds Ee EP 1 OR 2 002 94 27 95 Y x Lo 2 8 2re
26. 2 6 CDC 6600 TOSBAC 5600 30K 3 Redfield S C Morgolis 5 FORTAN PROGRAM FOR THE TRANSIENT THERMODYNAMICS OF PRES SURIZERS WAPD TM 545 19 1 10 3
27. ewt 1 0 4 Di 0 Ki 0 OIRO 0 0 0980940 00 09 0 00 0 0N 1 07 07 00 Ar CO 07 lt 0 07 56 4 0 1 8 00 0 Hr 4 0 Ce Y x y 0 gt 9C YLIK 5 5 7 sin 0 0 R RO 0 140 0 cos 0 VERR Green Wehausen yix yix 1 rz h ekhcoshg h y Cosh CT 0 k k sinh Kcosh kh ekgh sinh Koh cosh Ko cosh
28. 2 4 2 1964 350C 1 lt lt 175 350 300C lt 7 lt 375C 9 2 4 3 2 47 E J PAT T 0 01 lt lt 374 15 PAS
29. T TGW PH P OD G W 48 DT 244 2 2 5 2 20 Fih D 2 6 2 0 1000 0 01 800 0 3 0 Kcal kg K 0 800 bar 0 700 0 500 0 700
30. 4 9 J sa wa 2 9 2 p 3 3 h 9 Ts f Pv Ts eee 4 5 55 6 6 7 8 46 1 0 lt lt 2 0 lt 0 lt 0 8 00 6 0 lt 1 0 2 8100 2 100 lt 8 lt 3 0 0 1 lt 80 5 600 KBI 4 0 8 8200 2 150 lt 0 lt 81 0 lt 8 lt 3 0 lt 0 lt 0 0 lt 8 lt 8 2 1 9 1 pO BLO 1 3 2 1 2 6
31. 1 Nal 1 10MeV 100 2 E MC33 GCOS MC33 2 2 1 MC33 MC33 2 2
32. 1 PR PROUT 2 10 2 2 1 2 2 15 16 2 3 51 2 2 4 K 1 2 5
33. 2 11 12 Owo e sin a _ bian jn 7 g 7 gg7 7677 2 T 2 Ko fr nl aT REEE lsr fRislfRi 7 7 tolby CSa l az 1 2 2 1
34. 1 48 49 1 69 24 3 548 2 21 2 2 2 3 50 4 7 2 4 Over leve Band level 5
35. Arbitrary Motion of Submerged Circular Cy linder 2 2 2 3 50 10 2 4 S 9350 1 9 6 Da 1 4 y4 0 pl sin vgkt E ds 0 T x fo EDI sin EX 64 1 1 0 Fre dholm 06 7 0 1 9 2 5 2
36. 1 1 4 30kW 2 1 5 75kW 8 2 2 26 1 3 Box SUBRUI CALLE SUBHIND 2 98 CALL SUBAX HIERRO RETURN 2 4 27 2 5 3 2 4 5 CALL SUB HIND CALL SUBAX 63 8 000Hz 8 4 No 0 1 15 Nal
37. OF 3 2 2 1 Fourier Analysis of the Datac Data 2 2 8 2 3 51 12 2 4 1 2 5 TOSBAC 5600 FOUR02 3
38. 2 3 51 11 2 4 eg START ERR JLT Pers t DKaX 13 2 5 1 2 6 32 32 18kKW 3 2 BAER 4
39. 740 2 40 3 Diffraction Lewis From 6 4 Yu Ursell Kim
40. 44 T amp 4 1 ii iii 9 1 i 11 v viii 2 5 1 At
41. Tony yi 2 5 1 2 BLOPRE 2 6 TOSBAC 5600 FORTRAN 20kW 29 30 MDYCR1 2 Mi D ak A RETURN 54 2 3 BLOPRE MDYCR 1 Moody 4 1
42. 27 28 2 3 11150 2 2 4 Grodstein McGinnies 2880 O biparation Kahn Zerby amp Moran 50 2 5 1 1
43. 500 bar 700C 800 700C 1968 TSME JSME KORAN 2 2 1 STEAM TABLE 2 2 2 3 50 4 2 4 2 4 1 2 7 h 9 9 4 Gibbs J Helm
44. 1 16 2 6 TOSBAC 5600 10kW 3 3 1 22 26 bR 90 3 2 2 3 1 3 3 m 3 301 10 Ds01 02 05 hs 50 ba 17 09 0 260 0 6n0 400 7 11 3906 0 0 206170 ZUGD 15649 644 UUU y 892489 80097 200270 0 0 nto r 900 _ CO 480T D 351270 77848 UUG 44 UIGU 914 8 EN 02270 Str 0 20 342170 3 6070 8 99 6 gog 0007 ui u 9848 2107 20
45. 3 2 3 3 RAA hi ER U AA 1 lt gt 5 10 2 1 2 EES 4 2 1
46. EB 2 2 2 12 eica ERal 2 5 2 K 6 index 26 TOSBAC 5600 60KW 3 4 2 0 5 10 0 KB 2 0 05 5 0 15 0 90 MT MT 1 8 lt 11 17 1974 2 126 1969
47. SECTIONAL CRANKSHAFT 2 2 2 3 50 9 2 4 FEM 2 5 1 26 FACOM 270 20 TOSBAC 5600 45KW 21 22 AR 210843 Yes 0 1
48. 1 Shah Kobayashi S Stress Intensity Factors for Elliptical Crack Ap proaching the Surface of a Semi infinite Solid Inf J of Fracture vol 9 No 2 June 1973 10 1 2 3 2 21 CALCULATIONS OF PLANE STRESSES AND PRINCIPAL STRESSES FROM MEASURED STRAINS amp 2 3 2 3 2 3 BG L 1 nN 1 2 2 Hh amp 3 lt gt YES 2 2 33 2 3 51 11 2 4 1 THE TARLE OF THERMOCHEMICAL PROPERTIES CP CVH
49. 1 1 0 518 EMeV 2 1 28
50. gt 9 2 9 2 4 kam 221 45 E CTE 2 coS 0 2 sin 0 f dk 0 2 CHOICE 22 2 3 9 3 2 SOU v v 25 2 2 6 TOSBAC 5600 20kW LP 3 TOSBAC 5600
51. expricit ARRE START INPUT DATA Time Step TimeStep imeStep 31 2 5 1 2 6 TM 17kW 3
52. 2p u 1 hs 0 ha 9 7 P n lt lt 012 4 44 7 74477 4c44 7 4 26 4 2 0 1 9 0 4 1 T 4 0 2 7 711 gt 0 150 gig 3 2 90 exp 2 5 Gl Re 6 2 5 2 1 7 0 19 aa e 20 SUB Runge Kutta SUB ER 04 0 2 0720 30 20 IO 0 10 20 30 40 50 60 70 L 2 5 3 202 1 Runge Kutta 4 0 2 26 FACOM 270 20 30
53. DRIVE COS IOPT 1 COS IOPT 2 INT1D ORIFIC FLOWPD CIRCLE 2 D 2 3 total OUTPUT INPUT DATA PUMPPD Pump POMPPD Input 0 Pump Pump 38 2 6 TOSBAC 5600 21kMW 3
54. 3 11 1 5 49 1 2 2 39 3 1 E KE 2 2 1 Hydrodynamical Forces an Oscillating Cy linder in Shallow Water 2 2 2 3 50 7 51 7 0 gt 2 4 1
55. 3 1 3 2 RETURN SUBROUTINE DELTA SUBROUTINE TROK SUBROUTINE GART 230 24 START RITE R 2 REER AN RI 4 y SUBROUTINE DUV SUBROUTINE RDETAM R 3 RES 0 C DRR lt 0 ROJE VAI NRR TIY 2 m SUBROUTINE PROC
56. 39 1 N SR 7 47 2 3 20 1
57. 12 1 52 1 p 55 60 23 13 gt E 1 ZOLAR 2 2 1 2 2 2 3 51 4 2 4 y Hia PROC k o
58. 45kW 60 11 230 500 FORTY ACTIVITY 13 3 4 2 mD 4 IFLG 1 6 1 11
59. cos 27 T ITI gt oa ana l T Tin eosh 7 T 08 J OI 1 In eosh _ 9 gt 0 Dg s 2 7 0 2 5 2 2 6 TOSBAC 5600 EOR RKAS DU Simpson 5 INPUT DATA Lewis Form Green
60. 8 d d 9 2 e 10 f 33 34 16 Pump 1 7 Pump 15 Between and Pump gt 14 Suctron Hole Outlet 18 Pump Diffuser s ael J 13 Suction Hole Inlet lt 19 pump Diffuser Outlet lt 20 Between Diffuse 12 1 5 Sup 2222 11 Grid 10 0 Grid Outlet 21 Steam Generator i 9 Upper Grid 4 Plate 8 Fuel Upper BZZ ZA Nozzle 7T Fuel R od Outlet 22 Convergent em Under 5 6 Fue1 5 Fue1 Rod Inlet 2 4 55552 4 1 Lower 23 Comer 221 3 Lower Grid plateSSSSSN 2 Between Sup Grid Pt 65555 1 Lower Support j Plate to 24 Between S G L Support 1 34 35 814449581299 4 1444414 YY 643414 72
61. 10 3 1 s c 10 4 ee eo ar9 Two p ex 6 Ca amp 46 Criticel 64 0 0 0 4 K L 9 1 2 9 90 5 8 e 3 4 7 T 7 7
62. Subroutine 4 Hess 4 Smith Element D 26 1975 12 2 1976 2 3 Potential Hess amp Smith program 5 version 1976 10 2 2 1
63. 8 O 1 2 2 1 2 2 2 3 48 51 12 2 4 2 1
64. TOSBAC 5600 11kKW 3 21 2 1 3 4 12 1
65. y Ko K Ko x x Ko Kh sinh 12r K K tanh ra y 3 217 1 12 0 v8 B 2 0 1 0 0 2 Simpson 20 1 Green 9 6 9 9C 9y 2 0 2 2 3 27 K K cosh 3 cosh Ko _ 2 Mk Zzz tan 1
66. LL 19834777 9 LL6T 91 11 26 5 2203772 yt Ti LL 2 2 6 9T cg S 94544 99 4267 91 7 2645 97775777 9 TE 26 2 5 51 ow amit a 52 FORTRAN 1 DATTIM 1 6 3 3 1 CALL CALL DATPRT 2HAA 1 2HAA 2 S 19 b bb b 5 2 Gi
67. NETGHT FLOW RATE TONZHR 7 PUMP PRESSURE KGZCM2 0 KG DRIVING CALCULATEC FLOW RATE TONZHR 2 044006 GPTION 1 OPTION 1 aa FUEL HEIGHT u 2 2400 LENGTH 2 800 0 0310 HEATED PTPE DIAMETER O NIN8ER HEATED ROW _ 115 ABSOLUE PRFSS TOTAL I FRICTION _ KG KG CM2 I 2 KG M2 I HANNEL I INLET LENGTH 1 1 0 06650 _ 139 857 _0 07674_ 16 156 751 241 DIBI oara N 4 LOYER NOZZLE 130 684 0 15390_ 1559 014 FUEL ROD 84 6 FUEL ROD 2240 00022 379 805 2 ROD TUTLET 319 805 _ 139 505 28 124 865 cend Voan VELA UPPER NOZZLE 809 805 439 426 a 276 658 PLATE 805 2 10 GRIN OUTLET 509 805 0 00562 1 21 90 1520 200_ 309 805 159 361 12 ONTROL ROD 509 85 2040000 13 SUCTION HOLE INLET 309 805 159 360 0 97063 VA SUCTION OUTLET 805 139 331 0 02957 _ 295 743 4 RETEEEN SNU 9094805 4394801
68. 15 7 0 2 14 15 _ 5 CALL THRM 2560 0s4 ACP 74 6 104 5 6 102 4 5 6 104 2 4 12 10 12 44 15 _ 14 0 5X CALZK TCALZMOL 7 7102 2 5 5 12 5 2 1 5 2 12 END EXECUTION PROGRAM ENTERED AT 037736 THROUGH 4FSETU Ra r A CAL K MOL CAL K MOL CAL MOL CAL K MOL H _0 49660 01 0 29800 01 _ 0 65352 05 0 380746 02 47 1 1 1 1 2 5 2 6 1 1 V STOL G r tler
69. Gi 2 5 1 2 6 TOSBAC 5600 51 29 07 10 0 2 107 2 407 2 0 2 91117115 2343424 9 67 97 72 265 5 9 TT ZL 9111111 95 11 66 20 245 29207 9 1114 29107 9117114 6 91 724 5 29 07 9 4 Zvint 9 7 6 7 0 974777245 25107 97 11 1 6 1 01 9T TLL 2 0 6 0 17 25 5 tT 9 97 9 9 evnt gr gt ZLL6T T CS 9 TE LL 11 446T gr LL 1 91917444061 9 I Or LL 9 07 DTTT LL EriUT 0 Zy30T 97 TT 9192 0 gT 0 91 9 07 ar t 0 744313 29 0 443944 05 61 5 4 ZZ ZZ6 2 15444773 ITST LLa 9T TL LLOT 91771172575
70. NO 25 26 FENNO 2 Ton Box 590 5 CSAR CALL SUBA CALL SUDBB ZNO 1 2 CALL SUBRDUI CALL SUBC NO 2 gt 9 85 NO A o YRS RETURN KARRE REC RETURN 1 4 1 9 2 5 1 1 4 2 1 5 2 6 TOSBAC 5600 FORTRAN
71. 1 49 1 2 51 11 3 3 49 K 15 K SBRTN STRES KK OPRGD SMAT CK 4oKe l AINV 4 NO gt YES lt NO IFLGUS1 lt gt Pi NO IFLG 3 6 K LP 9 K K 5 Kobayashi 20 ERORE GEBR
72. 2 52 0 136 0 0 3 2 2 3 3 1 WRITE 4 1
73. 3 3 1 FEM 22 Time 15min 3 2 2 4 1 1 50 2 41 3
74. 1 8 4 TOSBAC 5600 11K 273 J SMEO RAR 1 1968 2 34 265 43 9 1567 49 22 Ch 5 1 Cp Co S J ANAF
75. 157F 42500 410 OTT 7777 0 606706 01 0 45000 01 0 66507 041 0 455006 01 0 60 64 01 6 44000F 0 0 448008 0 597516 01 _0 45000 01 0 59145 01 0445 0 01 0 58699 01 0 46000 01 0 58402 01 0446500E 01 6 57522 017 0 470005 01 09575368 01 0 475008 UL a 0 57100 01 0 48000 01 0 56634 01 0 48600 01 0 56495 01 0 49000 01 ______ 562 01 222 2049 04 0 969406 01 0 500006 01 70 56 85 01 0 01 0 562986 01 0 5100 1 0 51500 01 5665 01 704 01 0 556166 017 Calculated Result T 274445 PROCES INIAL ITMEAN SYMPSN TRAPEZ 420
76. 01 0 69765 01 0 24500 0177 99762 01 0n 25CnOE NL 08 69299 01 0 25500 01 0 6156 01 Q 68436E 01 77 77770 681536 01 n 27nn0F NL 0 68040 01 0 27900 01 8 24 01 70 28000 01 0 589716701 0 255n0E_ Ot 1 68051 017 0 29000F AL 067699E 01 0 295008 01 L 0 47476 01 0 SnonnF 01 0 67 259 UL px30500E n1 0 67159 01 0 31900E 01 66958 01 O OE 01 667186 0 9 320002 01 6 01 0s325n0E 1 0 66385 01 NANE 01 0 6179 01 0 535006 01 0 05890 01 777846 CALCULATION OF MEANVALUE OF FANCYION F ENERGY 451 INTEGRAL 565 99 PINIMUN VALUE EFFECTIVE 0 936E 00 MAXINUM VALUE OF 0 lt 148E 0 WIDTH INTEGRATION 0z259E 00 CONSTANT 9834990F 01 01 0 545006701 LELEI 01 0 450006 01 64560E 0 858008 04 064490E 01 01 70 641474 01 0 36500 01 0 64679 01 0 870808 fs 694776 01 0 875008 01 0 653696 01 01 0 830746 01 38500E 01 0 62841 01 0 9 01 0 625 9 01 04895005 11 0 622226 01 4nnnnF AL 0 61749E 01 0 40500 01 0 5166 701 0 410008 01 90 61567F 01 0 415 0 01 _ 0 61715 01 px42009F 01 O UTT
77. 1 Mises 38 Prandtl Reuss 13 14 2 4 4 451 0 1 0 4 4
78. HX EE TETAK 449 7772 5992655 19495 7762 21 71 5 2 P S EETA ATA 941414 27 2 ES 2 77 1 4844071 77V 35 3411004925 0 gt anla gt 94 77 94 975 77Y 44 4 94 971 77 21 4149 27 02 27 1 Ledadid 44414 gt 41974 4 77 9 77 0 CLS 414 44 974 i 5 2 3111954975 094805 36 8 9 Tavis ddd 211130 314004915 3 4004819 a QILNI _ 00 30114004805 3414194915 E NAN LAY 0024405 3NLOoag0S 36 37 a NATURAL CIRCULATION CALCULATION INITIAL CONDITION o
79. 1 6 0 6 44 yog orr 09974 0896709 ST OU ing 20 369770 0 30160 698 2799 66 uuu gy T SIDD vI no y pIu TALYU 32309700 97 5 2 UUg 9 uusi Gnp yg 11041 0 0 30608 0 Uyot pre UUU L G U 6 ye Uro TO 620 3092 100500 1 0 U 41971 20 4996 U 57906 UUU US 0 rit ty P L AU dS e us ULE 0UU9 1090 Luebp_ 0 0 20 20 960 0 978126 6 9 91 uot UUU amp uns U Hp 6 Cny pnz teit TEO T 2 420970 pb 6 LS 6 UNGU upu u 2 0 0 US UIg y 66 44 m PRU MCU OM UUT wed 930 Ghot U Puate UUU tt UIG UY LEU Y Yt Ug U be UE ZU T 00 Et CU H06p 0 go 5 uc
80. 4 amp 3dYaL anIA20 go 8 0 4 2421 4V4 lt 1100905 Na2133 6 5 6 6 9 VLS vs 935434 WIND 7 224405 3 4094305 3271100975 41 42 FORMATION INTEGRANT 157 5 1 ENERGY CALCULATE 516 AT EVERY 0 506E lt 61 WIDTH INTEGRATICNZDEVIATION Er Input Data List ENERGY ___ __ ENER6Y __ SIGMA LE 0 158010 001724222 6222 60106400 70402 77 059365 0 13000 93 0 69027 01 22220115006 01 ___ 0 69600 01 0 120707 01 OL 0 125006 01 777 0 69542 01 0 130700 03 _ 2220 69 01 _____ 204136006 01 1 0 69442 01 0 14000 04 0 68767 01 0 14500 01777 0 69614 01 0 150 0 01 0 68966 01 0n 155n0E 04 0 69471E 01 0 36000 04 0 6G8SS2E 01 07465m0FE 0 59756 01 0v170n00F 9 0 17500 01 __ 0 70242E 01 0 17000 01 0 69004 11 0 185 0 01 TT 701709308 01 0vi9nnnF 02172222 OE 01 0 71045 01 0 270006 01 0 69979 01 0 20510 017 0 71612 01 0 21119 11 0 70682 01 0 21500 01 0 71442 01 0022n0DE 21 0 70491 01 0 22506 70687 017 0 2xpnDF N14 0 70344E 01 _________0 25500 01 0 69588 01
81. SUBROUTINE PROC 51 1 242 51 gt 0 4 25 3 2 2 1 27 1976 17 20 2 1977 Tokyo Joint Gas Turbine Congress Pa No 25 1977 5 14
82. 0 050325 090 80 16 INLET 309 805 159 321 0 00702 0 188 4215 170 209 805 139 585 0 09441 0 507 PUMP_BTFENSER 136 2012404 DIFFUSER OUTLET 5985 139 545 0 09895 589 401 202 BETWEEN DIFFUSER AND SG 319 805 59909777 50 08098 11 25 521 016 2 22 24 L STEAM GENERATOR 280 000 309 805 ____ 0 __ 22 CONVERGENT UNNER SG o so 239 610 0 034866 0 008 2948 62 DDRN COMER FT EL EN 37 38 f 2 he 29 m v m sec BK 4 10 1 1 2 5 2 2 3 1 No 1 Lower Support Plate 2 Between Sup and Grid Pt 3 Lower Grid Plate 4 Fuel A Lower Nozzle 5 Fuel Rod 6 Fuel Rod 7 Fuel Rod Outlet 8 Fuel Upper Nozzle 9 Upper Grid Plate 10 U
83. 0 3 3 1 GRAPH 3 2 TT 3 10 4 5576910 19 az 2 gt 43 44 E T 10 V8L97 565 1955 CVRNS 4 SEY PHYS REV ssev a 559 01 GENEVA CBNP V6L4 22 1955 VLADENIRSKI 5501 2 55 3 III barm 44 45 21 1 1963 6 1000 bar 800C 1964
84. 1 TL G AL GT RETURN RETURN 1 RETURN 3 3 1 CALL I AS 1 298 0 6000 09 BLOCK DATA 1 6 11 Ar 2 7 12 O 3 8 13 4 9 Ne 14 5 10 0 15 AS Cp CAL K MOLE 49 50 MOLE CAL MOLE CAL K MOLE 3 2 WRITE BLOCK DATA 4 BLOCK DATA Thermochemical Data Dow chemical Co Ltd 23 1
85. 1 Thin Ship 1 2 2 1 Thin Ship Theory 2 2 2 3 51 1 2 4 Source 1 2 6 N M os OSE 1 F x 2 2n p 1 m i E A Z 49 f O y 221 tiv 2 2
86. 2 2 2 1 SUBROUTINE CIRCLE 2 2 BTH PIRRE 2 3 51 4 2 4 10 1 i i i mf Kcal 1 kg sec Kcal kg m 2
87. INPUT DATA 880 151 NT 1 1708 151 FBA REER lt 7 gati E OUTPUT 8 7 8 2 6 5600 30KW 3 4 D AREH 134 1973 2 S Ohmatsu On Irregula
88. Ky 4 00 1 00 3 0 45 2 Qos oo ye sin 4 sin 9 _ 7 1 3 6 560 Od QI j 7 1 3 64 0 bra or r j Sin X 7 7 1 3 6 Sin 7 z fi fR jkt 1 2 3 5 20 ds 7 CZT 7 061 __ 04 0 _ 087 95 0 o gt 7
89. S E P 0 0062 lt 225 56 4 P T v T P h TGPS 5 VGWPH v Taaha BARK kaxa veso SGWPH 2 HGWPS 65 XZGWPH H X Z gt 72 7 7 HLPT h TLPH P TLPS P 5 l CPPT 1 cr 1 e 1 7 2 P T I
90. bus U OSUU 9 t 040 0 179210666 6 0080 84076 19470 LR 0 eRT TU SE lt 9 0 ODT 9 0047910 00160 uyun 90474 06 0 ETTARI U oogr rE Uisty 648 69 p org 0 2 tou t 9 0 U B61 U 0 9 UUs 6F 09440 6 676 so u l ____ Bd BNd 20 i 541724220049 ZIN 4 0 2 006 G R A r og 4 0 4 lt 0004 A O a S419AO N ___ 050119 aNOLLIUNOD 1531 30 17 18 4
91. holtz Gibbs Helmholtz 409 85 21 0 1000 bar 0 01C gt 800 6 2 1 1 4 5 8 0 hI Perevet gi oy Pc
92. pper Grid Outlet 11 Between Grid and Sup Pt 12 Control Rod Sup St 13 Suction 14 Suction Outlet 15 Between and Pump 16 Pump 17 Pump 18 Pump Diffuser 19 Pump Diffuser Outlet 20 Between Diffuser S G 21 Steam Generator 22 Convergent under S G 23 Down Comer 24 Between S G and L Sup CIRCLE gt k Jk X 180 SopS 2 o PIPEPD Option KD 1 1 ID 1 1 Blasuis ID 2 ii Rander KD 2 2 VENDPD FLOWPD ID 1 ID 1 gih _sLOWPD_ ORIFIC COREPD SGPD S G SGDIS 8 G
93. r Frequencies the Theory of Oscillating Bodies in a Free Surface Papers of SRI 48 1975 D 51 1976 5 1 MT O MT 3 M Fourier
94. uk UUg ungu Su 6 Le LU OO ycCc ti teu I 1 0 5728606 6 UUG D yl 0870 9470 teut 1901 20 3946 0 wu 3dyba U bdcc beu tu dt 01970 gr Or Qb un 19977 6 3 1970 0 847996 gr opP 994790 764 0 u DO T U d LZ U ule Lv 139 ug UUU UGU U f 00950 960 0 564 0 99 0 9 0 fL F 2 0 0 960 0 97142 Gry 19 Livo va u UL 09 0 5 0_ 4 7 66 195 pge 0 6 6 p 09970 0 LT 0 329670 IO 9 UUU L 0 6 96071 Y t 890 BETOL APOTE L APOTE LE ET UL 2 9 u Lyt 9LC 6 0997495 6 4 00470 0 tu T rit 0 et U U cle pr Lee 9r UUU Z 0060 UL 299 121 10 6 0 LILL LT
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