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64. 4 2008 Pilot project for environmental technology verification Technical field of organic wastewater treatment for small scale enterprises Technology for organic wastewater treatment in small scale enterprises kitchen restaurant and food manufacturing industries The report of result of experimental verification Outline Demonstration institution Saitama Environmental Analysis amp Research Association Environmental technology developer SEISUI Corp Technology product name Mecha cera device type SDO A 100 SEISUI Corp mecha cera device Technology verification environmental Ceramic device type SDO A 100 SEISUI Corp technology developer Demonstration institution Saitama Environmental Analysis amp Research Association Period of the verification From September 18 to December 4 2008 experiment Application of aqueous solution that contains free chlorine CIO to a ceramic or mecha cera ball that acts as a chlorin oxidation catalyst activates free Purpose of this technology chlorine and produces nascent oxygen with a strong oxidative effect Mecha cera is a system that is effective for reducing the volume and deodorizing sludge with the help of active water that has sufficient oxidizing capability 1 Outline of the technology to be verified inflow section 8 Incorporation slud ichi ti mms sludge enriching section In
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85. SS S S 5 6 165mg L 123 7mg L 73 196mg L 117mg L 185mg L 144 2mg L 82 218mg L 129mg L 24mg L 21 2mg L 15 34mg L 23mg L 2 8mg L 2 4mg L 1 6 4 4mg L 2 7mg L 19 5mg L 9 9mg L 0 9 7 5mg L 2 9mg L 10 mg L 10 mg L 10 16mg L 13mg L 10 14mg L 12mg L 1 1 1 8mg L 1 3mg L 0 9 1 8mg L 1 4mg L l 5 7 SH vil 8 0 L I vil 9 vil vit 8 0 LET VT S I 11 9 6 671 VT ST ST IT OT VI CT LI II OT II II el II II 19 CT OT II LI VI el el MOT OT OI OT OI OT MOT
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110. 8 0 100 0 000 7 10 13 16 20 21 135 emas ree Ive IEE AND edi 5 10 10 mL nf ni mL nt mL nf 11 15 11 16 11 17 11 18 11 19 11 20 11 21 m h 1131 0 814 0 814 345 0 124 0 124 601 0 433 0 433 m S e S S S lt ooo ojo S S S S S S S oo ooo S S ii m s s m h 0 814 m h 1 000 r 1 19 5 m H 0 900 0 800 0 700 0 600 0 433 m h 1 10 4 mT 0 500 CA 0 300 0 124 m h 1 3 0 mT 0 200 O00 5 0 000 11 15 11 16 11 17 11 18
111. 173 2T 202 8m 9 139 7m hess 22 184 4m 250 0 200 0 150 0 100 0 50 0 6 66 6 86 6 12 6 96 6 1 66 6 1 76 6 1 6 6 1 66 6 16 6 02 6 61 6 81 6 21 6 91 6 91 6 1 6 61 6 61 6 11 6 01 6 6 6 8 6 2 6 9 6 9 6 7 6 6 6 6 6 1 6 o sem 10 m H 250 0 174 4m 200 0 16 01 06 01 66 01 82 01 46 01 d 96 01 4 6 01 01 4 66 01 4 66 01 4 16 01 4 06 01 1 61 01 d 81 01 d 11 01 1 91 01 1 61 01 1 71 01 1 61 01 1 61 01 1 11 01 101 01 6 01 1 8 01 2 01 9 01 9 01 7 01 6 01 6 01 1 01 E 11 m H 250 0 163 2mY 200 0 06 11 4 66 1 86 11 A 16 11 4 96 11 SEPET 11 11 16 11 1 06 11 1 61 11 3 8I II 4 I II 9T TI VI TI LEI 1 11 TI II 1 01 11 1 6 11 4 8 11 21 11 9 11 Sr 1 6 11
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113. me 10 4 1 2 With You 3 20 EES 4 L 5 6 1 2 3 4 21 2 26 14 00 16 10 1 20 8 18 H 14 00 17 00 2
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115. ae MMSE A X A 4 3 92 4 4 4 2 4 2 1 3 kg 13 20 50g 6 1 50g 6 1 11 2kWh 289 6kWh H 4 5 4 3 9 1
116. vw a OO TM NO Nsw ON OWN NM FO DPR AO ON CO CO SISIN P OO or ololol oo oolo 2 gt Cleo IO ES SS qoq SP OO IN DT E G0 Bo oT AI OO CO CO OT OT RFR OT Nj oO Olof ol MIR UO ajaj Si 115 H H19 11 22 H19 11 23 H19 11 24 H19 11 25 H19 11 26 H19 11 27 H19 11 28 H19 11 29 H19 11 30 a 6 00 18 00 X 18 00 22 H 6 00 n H un rR c O 5 N CD oOo Dm oye CO MT O nl olo no ON NIT O O HE E ON E O COT E A O ON PO O E O O OER OO no c ros w ol ln
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118. SS SS 11 20 11 20 11 20 11 20 11 20 10 13 16 206 216 2 AKT 1 2 142 KEP 1 2 3 1 2 Ex 1012 358 TETER Fae ie NA AT Pa TE in Bee a EAT ATS 1 E FEAT EAE BO ORP 1 2 1 2 K ste ETS CEE 2 3 fe Aik to Ste 1 2 LEIS gR HA SS 8 220cm 130cm ai ee m 9 18 1 2 1 2 2 cm
119. 3 11 1 T 2 2 20 11 14 8 S 5 28 000mg L 2 909 97 19 1 S S 30 700mg L 3 159 96 8 2 SS 37 800mg L 3 80 96 2 5 8 20 6 20 9 20 11 SS mg L 28 000 30 700 37 800 1 12 16mT 20 7 9 3 7mm 75 20 10 11 7 4 m 509 5 5 18m 659
120. 5 9 20 7 20 8 20 9 20 10 20 11 ig 75 0 75 0 50 0 50 0 33 S S S S Puce pak oe A AIO BE ORRIO S 15414 40kg ToD 20 7 9 SS 113 59kg S 5 72 6 20 10 11 SS 279 72kg S 5 32 59 5 SS 177 42kg SS 57 29 ke SS mg L 5 10 SS SS 20 6 20 7 20 8 20 9 20 10 20 11 ee ee e l S S mg L 30 700 30 700 30 700 37 800 37 800 34 250 m 3 7 3 7 3 7 7 4 7 4 5 18 SS kg 414 40 113 59 113 59 113 59 279 72 279 72 igr 42 SS s i 72 6 7
121. 20 10 11 7 4m 509 6 5 5 18m 659 6 20 6 20 7 20 8 20 9 20 10 20 11 96 Was 75 0 75 0 75 0 50 0 50 0 SS SS SS 414 40 kg 20 7 9 SS 113 59 kg SS 72 696 20 10 A 11 S S 279 72 kg SS 32 59 6 5 SS 177 42 kg SS 57 2 SS kg SS mg L x m SS SS FU FU wT ct 20 7 11
122. H H ES DF 4 1 4 1 WW rm UE Es E Eo i H E EE IR 20 1 2 3 4 a S cO ka E ma HE TREE lt lt H m m X lt KKHH X K Hmm CN LO O cN C LO CO O O M F LO CO O III I N CN CN CN CN CN CN CN CN CN OD r 20 lt K amp H T m lt X K ase s a Q Q Q Q QS S lt Q Kal ae i 20 BIR XK Hmm X lt KH mm e H mm XX KH OX CN CO LO cN C LO CO CN Tt cN CN CN CN CN CN CN CN CN CN GO 12 4 2 1 15
123. J S kal TERE x GN AE LY y YN 2 4 TER ON y W IN Wy ELAM oe lt APA 6 j x E dy ESS HORE y H 77 ue JAL N mM F lt T EEN LA V ware J J a I YTA ADOT 2 Pa IN LUXY Z d ae 5 gt I Ee HAVEN 44 N Ry mm HH g Q UK ae U m a tk HE LO a O BU MH jp O I bf nu lt Gr lly gly p s gt 12 mm Ta 57 3 3 100L
124. 20 FE 21 3 O O IH HE a 4 NS 3 gt 1 ALE 2 ee 2 1 2 2 1 ET O OO e EREE 3 1 3 2 3 3 cece cece eee ee cece eee eens 3 4 3 5 4 C 4 1 ce ec ce eee ee ee eee eee MS EN EEA 4 3 Ate 5 SS sa a Seed
125. Dis 5 r sees t u bd Y p m lt lt m m K oe K x wy as 7 gt li O gt Kap mp E H FE 4 o TOMO 1 27 x 7 1 2 1 9 gt Ww 1 l l 6 6 7 9 11 19 21 23 0 6 12 18 All Meri 3 3 87 4 4 1 C10 NaC10 C
126. Outline 1 SEISUI Corp mecha cera device 3 Results of the verification experiment We measured the amount of sludge before and after the verification device was introduced to compare the values The amount of sludge was 14 8 m in June 2008 when the verification device had not been introduced After the device was introduced the amount of sludge was measured twice The amount was 11 1 m in September 2008 and 14 8 m in November 2008 Regarding the sludge properties SS was 28 000 mg L solid content 2 90 and water content 97 1 before the device was introduced After the device was introduced SS was 30 700 mg L solid content 3 15 and water content 96 8 in September 2008 while SS was 37 800 mg L solid content 3 80 and water content 96 2 in November 2008 This result showed that the sludge density increased and water content decreased after the device was introduced Amount of sludge and its properties before and after the introduction of the verification device Month when sludge was carried out June 2008 September 2008 Novenber 2008 ee before device after the device was introduced was introduced 14 8 2 1 8 Since approximately 12 16 m3 of sludge was regularly removed once a month before the introduction of the device we 1 1 1 used the data for June 2008 to represent a standard value and determined the volume loss rate of sludge by calculating the amount of sludge per month after the
127. 1 2 3 11 20 1 2 3 1 A 55 F zk 5 2 A f 55 F zk 5 3 55 F zk 5 4 Boa A 55 F zk 5 5 A f 55 Rake 6 He OT U1 NN UO orn on CO OU CO P MPO PI HIN DW WIN oy os Rs As O Jodo gt gt gt 130 55 FK H 9 18 1 C lt aH 2 3 9 30 1 2 3 10 16 1 2 3 11 6 1 2 3 11 20 1
128. 3 95 RII 5 2 20 9 18 20 12 H 25 t 5 1 1 2 3 4 iE H tk 8 18 IE H 9 16 iE H 11 12 H 96 5 3 20 5 1 Paa 2 ITO GRIT FERRI LER ames 3
129. e OO OS H niy H Rw un 0N NS wn ol ol uo 19 12 1 ES lv H19 12 4 K 8 6 OO O H19 12 8 RM RM CO NI tS AJO el lt 6 00 18 00 C HIE s 5 18 00 H 6 00 it n H 116 0 0 0 0 0 0 0 5 0 0 0 00 6 2 6 6 6 0 4 8 oil 4 9 5 6 4 7 1 00 2 9 5 1 2 7 4 4 0 3 2 9 4 3 4 2 2 00 3 0 3 1 1 5 1 3 8 2 9 2 7 2 8 3 00 1 4 1 3 2 5 2 6 0 3 1 5 1 4 1 4 4 00 1 9 1 5 1 4 1 4 7 22 2 9 1 3 2 7 5 00 2 9 2 7 2 7 123 3 3 Leg 2 4 1 3 6 00 2 9 3 1 1 9 2 7 8 6 2 9 2 7 2 7 7 00 13 3 9 8 8 5 12 9 3 0 12 7 9 9 6 5 8 00 13 3 12 3 8 14 7 6 0 16 6 12 7 14 0 9 00 9 4 11 7 0 9 7 7 2b 12 7 11 8 11 0 10 00 6 3 9 7 11 0 8 3 8 8 7 9 8 9 4 13 0 11 00 4 4 8 3 10 0 4 5 6 1 6 6 0 6 1 6 9 8 8 12 00 4 5 6 8 5 9 4 4 6 0 5 4 6 6 2 6 0 5 6 13 00 6 1 4 8 6 0 4 5 5 0 4 5 4 6 3 4 5 5 7 14 00 5 3 4 3 4 6 4 1 4 3 4 6 3
130. r sm Wima 1 1 1 mg 1 1 1 1 1 n 1 on c HN BD O OR co O o tT HN HN DBD OR eo X A nN FN NF NNN SQ N NF FN G X gt NN X amp SN K Q S lt NF NNN 8 K Fran G x N os X HRN KY SPR NN q NN NN NA RN N ON NPY SS BW Ww YY NY DR VY ON DN X S 6 6 G G G fF F S S S FN S S S X 5 gt FY F X X XE lt FF KF KF NK eo eo eo E S X X X X X lt X X lt lt X NX S X S fF fF NNN gt XK gt KNX X lt K eo eo eo e eo eo eo e DH DB eo S S S N N N S N N N N N N O 8 amp O O O O O S O Q O O QO O 5 C amp S FF FHF NGF FH NSF ds S HGF SF FH O SS NNN amp amp 6 N O N N N N XN A KN A N N AN amp N N WN N N amp N N GW N A xn N Z a sm 1 9 2 2 34 32 30 28 26 24 22 20 18 16
131. 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 4 5 6 _ 59 Fk a 59 F zk a 59 F zk a 59 F zk a 59 F zk a 59 F zk a 111 20 I DIM OIS CO O U O WO WO O DM CWO DI OUFwlD WILD SDR WI WIV RIO OO CO O OO UO O II 126 1 2
132. 151 MS 47 50 5 10 2 ak ath oo RR EK ll FE 5 oe 21 2 3 1702 No 01 2009 2 2 amp A FB MLAP 17025 KES E 9 OMS
133. 200 000 TAKES 15 kWh 330kWh 3 000 1n 270 m HES 8 5m ODS
134. 5 SS 82 143mg L 114mg L 10 7 150 22 300mg L 12 214mg L EK SS 10 16 9 30 10 16 1 10 16 S S ARTA L CB L TW ED OREDOO SS 9 30 15
135. 1 2 12 20kg 1 2 2 1 2 2 1 1 1 2 1 2 75 lt COC 2 1 1 2 1 1 EDRI YE 2 2 1 2 40 8
136. 10 10 11 10 11 11 1 4 1 4 1 5 1 4 7 150 22 300 14 400 13 400 8 750 7 900 390 740 450 670 440 270 130 440 210 290 180 30 190 4 5 6 5 7 5 6 5 7 SS 82 218mg L 129mg L 10 7 150 22 300mg L 10 490mg L S S 9 30 10 16
137. i SD0 SEISU SEISUI CO LTD 50 F 2 gt y BRIE RST RAE IT OE OD Hy at AA Ss ke OEE HKA EE ISAS
138. 108 138 168 108 13K 168 Se O 01 01 00 O 30000 30000 138 ters 2 0 0 30000 30000 139 11 20 11 20 136 ae 2 11 20 ER EE 2 140 1 2 De ee BT Pa tee 1 2 ORP 1 he RTS RIS 5 1 ae 2 1 2 TER a 1 2 2 1 2 1 2 RE EES IEE E RES 2 LESS TAN f 141 SS
139. 11 19 11 20 11 21 4 136 Ua PERSP 10 10 nf h m h nf h nf h mL Ch lt m h G H m h 0 888 mi b 1 000 r 1 21 3 m H i 0 900 a gt 0 800 0 700 f 0 449 n h 0 600 1 10 7 mi H 0 500 J T Z Z u 0 400 0 300 0 136 mi h I 1 8 3 0 200 lt i 0 100 0 000 10 16 11 6 11 20 11 28 2 4 eK 137 10 9
140. 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 1 2 3 111 20 1 55 F zk 5 2 3 1 55 Rake 2 3 55 Rake 4 55 5 55 FK 6 133 55 F zk 5 E 1 A f 2 3 1 Boa A f 2 3 1 2
141. 23mg L 2 8 mg L 2 4mg L 4 4 mg L 2 7mg L 19 5 mg L 9 9mg L 7 5 mg L 2 9mg L 10 mg L mg L 10 16mg L 13mg L 14 mg L 12mg L 1 1 1 8mg L 1 3mg L 1 8 mg L 1 4mg L 1 2 1 1 _ Fr sa es
142. 4 14 35 RSA 10 5 12 5 REZONT Ne ae FPP FHMC C ERE DHE ZERER LE LIA MERE DALEK CH XDI KECE DDD D OBE LHR SILER E 53dB vidi HE JIS Z8731 5 11 1 37
143. FL 1 2 2 3 2 a NANT RATE Arete IK w 1 124 REAR PRAB IRIKAEe IRATE Je ZS Pas KEA 95 FR F zk PB HP 7K Be J Fk E pR E PAR PKR ba Sa R an S06 zz 5 2 3 1 2 si gD IENE it DY O O O O OL ii N it Naan 1 20 OTP HR OT WLW WFTW OTT HR OT WI C Ol OW U OOOO UO UO OO N wl CO CO wy nyo P Wasi Ds O1 I ES OT O O O sabo taa Ca E E ema 125
144. T N T P 108 lt H pH 7 71 pH F E cm 4 5cm Fh oN CN O 82 8 8002 12 8 8002 1 8 800Z 7 8 800Z IE 800Z 6 800Z 71 7 800Z 01 8006 800Z 92 9 8002 61 9 8002 71 9 8002 G 9 8006 6 9 800 6 6 8006 61 6 8006 8 8 8007 1 9 8007 be b 800 Ll b 800 01 800Z 800Z 7Z E 800Z 02 8002 1 800 9 8002 82 2 8002 12 2 8002 bl 800 L 800 IE 1 800Z 6 1 800Z 71 1 800Z 01 1 800 1 800Z 12 21 1002 02 21 1002 1 1 100 9 1 100 62 11 1002 eZ 11 700Z 61 11 100 8 11 100 1711 1002 GZ 01 L002 81 01 L002 LL 01 L00 1 01 700Z 12 6 1002 02 6 L002 1 6 L002 9 6 00Z pH 4 pH 3 UR cm 82 8 8002 12 8 8000 1 8 8006 8 800Z IE 800Z 6 800Z 11 1 8002 01 800Z 800Z 92 9 8006 61 9 8002 1 9 800Z G 9 8006 6 G 800 6 6 8006 61 6 8006 8 S 8002 1 9 8007 62 800Z Ll b 800 01 800 800Z 12 8 8002 02 8002 1 8002 9 g 800Z 82 2 8002 12 2 8002 1 2 8006 7 Z 800Z IE L 800Z 6 1 800Z 71 1 800Z 01 1 8002 1 800 12 1 1002
145. 1 CF 3 1 1 aver Een i lela efi mene wewee 1 S gt veces oo 3 1 2 2 r CEE makata I Ff 4 l Ju oo B lt fi m X wy gt o gt T hs B Bo Z H W R R m y g m i ffi i meea SHH HEH HFT z yo 1 2 3 1 2 13 6 op 6 E 20m CC L gt H 5 ane T 2 3 5
146. 5 10 00 5 8 7 5 8 18 3 8 8 7 7 4 8 8 3 11 00 2 5 6 5 7 6 7 5 8 6 1 0 5 6 5 3 12 00 3 5 1 cT 2 4 7 gT 4 5 9 6 1 5 4 13 00 1 6 1 2 0 6 6 2 9 4 6 9 4 7 4 7 14 00 0 3 1 8 8 4 8 2 8 4 8 9 4 6 4 4 15 00 i 4 5 5 3 4 4 3 0 3 1 7 4 5 4 9 16 00 6 3 7 5 4 3 0 4 3 4 5 6 3 0 4 5 17 00 4 3 1 6 8 4 4 4 2 4 8 T 4 7 4 5 18 00 8 7 0 9 1 6 5 5 3 7 1 9 6 7 5 3 19 00 4 9 8 0 5 7 5 8 5 10 0 5 8 4 8 7 20 00 7 14 4 10 3 9 1 8 7 0 8 4 9 8 21 00 8 9 5 8 1 9 1 8 5 22 00 9 4 8 7 8 2 8 2 23 00 5 4 0 6 3 8 9 m 165 5 165 3 163 1 153 1 162 8 146 6 150 6 154 4 136 7 160 2 113 H19 10 11 H19 10 12 H19 10 13 H19 10 15 H19 10 16 H19 10 17 H19 10 18 H19 10 19 H19 10 20 6 00 18 00 18 00 6 00 ae I Wit m HB leje NINI Alle c o o ol oo lt S S F o D co O O Om Prt Re C CO alalola ololo alo N Llo gow ou colle e e Co Co Nolo0 wo Ro Rl c e olas o oa SN ov OL ON OL
147. OO to rt Slo GO SS SS ROT E OE E R S E 1 20 oR Ro oe en 5 2 00 OS OI TO OI ES ola ana RR OIE O C U1 O sl pusa t aqa qos kus s oe Ps c wm s no SO e Se SS wow S CD OS MR OO C AJAn WP A 4 ee SIES CO N H19 10 22 H19 10 23 H19 10 24 H19 10 28 H19 10 29 H19 10 30 H19 10 31 6 00 18 00 a l THS 41 18 00 m H m OO OU NP CO ajv OT WO aJ Aol OTE NI NIN Ofa CD Boa asa s osa Su ksaq om DJ h me CD un on lo mo BR Role Alo lo 1 ol o H N h 99 P 4 Ol DIN co mE
148. pH BOD pH mg 0 8 6 r 20 9 2mg 0 6 9 9 2mg 8 2 7 8 T 7 4 F 7 F 6 6 F 6 2 F 8 l l 0 l l CO lt H OO LO ST CO OO LO a EE lt H lt N O N N N N N O O N N N N N N m N A m T m SS C1 mg mg i 30 r 60 25 H 50 f 90 40 15 1 9mg 0 30 10 20 5 10 F 0 0 CO CO LO CO 3 2 CO LO oD o we se eS an lt N Ww KY oo sss z z S c S S S S S mg d 20 p 18 16 14 12 10 8 6 4 F 2 0 I I I I 19 9 6 H19 10 4 H19 11 8 H20 2 7 H20 3 27 H20 4 10 H20 5 8 H20 6 5 H20 7 3 H20 8 7 9 3 1 H19 11 8 2 7 H20 3 27 H20 4 10 H20 8 7 4 5 pH BOD SS CI
149. 1 F E 2 1 2 1cm dos rB SS SS 146 SS SS SS SS SS SS SS SS SS SS fete f ib rH 10 10 1 2 od I 7 I 8 ZAE VENEER 147 10 11 20 11 11 1702 No 01 2008 11 5 fe P m E GAR CER AR MA KEE e A QMS NC 2008 11 11 ABB 1 P 2008 11 5 H k D TIS0
150. 1 5 2 4 8 6 9 6 5 6 8 12 00 4 4 8 6 4 7 7 2 0 5 0 5 1 4 9 5 2 4 9 5 3 13 00 6 7 0 4 8 6 9 2 7 3 6 3 6 9 9 3 3 2 5 9 14 00 3 5 3 4 7 3 6 3 0 5 0 5 1 6 8 6 5 4 7 5 3 15 00 8 4 9 6 3 2 0 0 5 5 2 3 2 4 8 5 4 4 7 4 6 16 00 4 6 0 6 4 1 3 22 4 6 4 6 3 0 3 6 8 0 4 3 17 00 3 3 8 8 1 3 7 2 9 4 3 4 7 4 4 5 6 4 8 4 5 18 00 6 5 1 8 2 7 5 6 8 5 5 7 4 7 2 7 2 5 3 6 8 19 00 9 9 5 13 2 8 9 9 6 8 9 9 8 9 3 6 1 9 8 9 2 20 00 9 9 9 13 0 11 5 11 7 9 4 8 0 7 8 8 4 9 0 21 00 9 9 9 10 6 8 5 9 6 9 5 9 7 TT 8 5 22 00 8 9 5 8 4 6 4 9 9 7 4 8 4 7 5 10 1 7 8 23 00 9 7 2 4 8 7 0 8 0 Teal 8 0 9 8 8 3 6 3 AR es 2 eee ee eee eee eee ee H19 10 2 H19 10 3 H19 10 4 H19 10 5 H19 10 6 H19 10 9 Ie J K 6 00 18 00 a ERE x lip HERFA SE EAS BEBE PNR Se 18 00 6 00 HFA E BRIE A RFN FRR m 0 0 3 5 0 0 0 0 4 0 1 0 1 5 0 00 5 0 7 1 9 2 6 5 6 1 5 i 5 0 4 7 1 00 4 2 4 7 3 1 3 1 2 9 5 1 3 0 3 0 2 2 00 3 8 2 9 0 1 2 9 2 9 9 0 2 9 1 5 4 3 00 2 5 1 4 0 4 SN 2 6 4 4 1 5 2 9 0 4 00 1 8 1 5 0 0 1 4 1 4 8 8 1 4 1 5 2 5 00 1 5 3 0 0 0 1 4 1 4 9 5 2 3 1 5 6 00 3 3 4 0 4 6 4 7 8 9 3 9 3 8 2 7 00 8 3 iki 2 7 11 4 5 11 7 10 6 8 5 3 8 00 5 12 1 1 1 14 4 9 14 8 7 10 7 8 9 00 11 0 2 3 11 6 4 9 5
151. 14 12 10 O N A Q D gt O C lt H LO cO CO O N lt H LO CO OO 9 N N N N N 31 0 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 D gt A IK 1 0 5 Vi 1 ED SVEN NANT PATA OBIE 1 6 2 quel VCMT ROPER ae AT 0 6 A 12 18 B 2 1 9 2 3 19 9 12 H 111 H19 9 10 MI 18 00 6 00 PE mi N 1 MW RS o al c rto c o asas Es EZ Sse Lag FS BETES C CO CO INI RK OT DO S OI U PSS IS CO CO AO NIU OS O cC o N j ORO CO CO alela SAnS Oo j N eA InN e IOO oO WO OOOO WO i kes gt
152. 5 9 5 9 _ ORFEO O vY C DFT AF Fax eo a eps mae me 28 2 aie ARTS 103 6
153. 5 6 5 8 0 6 2 19 00 5 8 0 3 8 2 7 8 7 0 7 7 20 00 9 8 2 0 7 1 9 2 8 4 9 6 21 00 3 9 4 1 8 4 8 1 10 9 8 7 22 00 5 0 0 4 0 9 0 7 2 23 00 27 0 9 6 3 I AAR Tt is gt ss i a eee H19 12 22 6 00 18 00 RE 18 00 6 00 i x mi BS E E EES lt e c e s v o SS lt S PD 52 BATE _ e e e bjs e sr wy ololwl ol un tol lt S co ol ol 1 O OF ES YI OPN IT RIT o IS EES ean P um sa sS Bl IP i do ON PIN 1 So Oo CD gt nN OP lw NT OT CT HR OLD CO Oil nN ean j joj CD S e C ov Null un e
154. 8 1 H20 4 1 H20 5 1 H20 6 1 H20 7 1 H20 8 1 28 T N 9 Jy T P 9 1 1 9 1 1 mg 0 H20 4 24 H20 5 22 H20 6 19 H20 7 17 B O D SS LEF T N U T P 107 mg 0 B O D mg 0 S S 20 p 19 5 10 18 9 14 7 12 10 ee ce rrr rr errr re Tere ee eee eT COLT oS Sees SS 5 1 KT 8 4 6 3 4 5 4 al 2 1 0 0 H20 4 1 H20 5 1 H20 6 1 H20 7 1 H20 8 1 H20 4 1 H20 5 1 H20 6 1 H20 7 1 H20 8 1 BOD SS mg 0 eee T N mg 0 T P 20 5 0 18 4 5 16 4 14 3 5 12 3 0 10 2 8 2 1 4 1 2 0 5 0 0 0 H20 4 1 H20 5 1 H20 6 1 H20 7 1 H20 8 1 H20 4 1 H20 5 1 H20 6 1 H20 7 1 H20 8 1 22 T N U x T P 9 1 2 9 1 2 0 0 H20 4 24 H20 5 22 H20 6 19 H20 7 17 BOD S S
155. 8 9 4 3 2 8 2 00 2 6 1 4 2 1 2 8 2 7 8 1 4 57 3 00 Def 2 6 2 0 1 4 1 3 3 1 4 4 00 1 2 1 3 2 6 1 3 1 3 7 1 3 1 3 5 00 2 6 1 3 1 3 2 8 1 3 8 1 4 1 3 6 00 4 5 4 2 3 1 2 8 4 4 2 4 5 4 4 7 00 9 13 4 9 2 9 5 13 5 11 9 5 8 00 15 4 13 1 13 5 13 5 5 15 0 6 9 00 4 9 5 12 7 13 0 9 6 9 12 9 7 10 00 4 8 4 8 8 11 7 6 4 1 7 7 4 11 00 3 4 5 6 3 8 7 4 4 8 6 2 8 12 00 2 4 2 6 2 5 2 5 7 4 4 5 13 00 5 18 2 4 4 5 5 5 0 5 20 0 52 14 00 SI 6 2 4 2 6 1 4 8 1 6 4 15 00 1 4 5 4 1 4 4 4 3 1 4 gt 16 00 8 4 0 2 8 4 4 2 9 4 4 5 17 00 3 7 6 2 4 4 4 2 5 4 4 18 00 3 6 3 6 7 8 5 6 4 3 6 6 19 00 1 7 8 8 9 8 9 8 8 1 7 28 20 00 6 8 1 8 4 9 0 8 4 6 8 9 21 00 oT 9 3 8 5 8 7 8 7 8 9 9 22 00 8 4 9 0 7 1 9 0 9 3 23 00 I 10 0 I si 2 5 6 i 2 ZE ___ ee H19 11 12 6 00 18 00 18 00 6 00 n H Bee s NN gt ODD E BE OND O oeo oeo coeo co NAN r PN PN wl 3 3 o PF cilo RT Rl
156. co o ul ol ol Ww ollo a n Nn o AJIN al ajaloo so S GO sO OO Ee E fe OO SS sO 9 S QS RP SR wl OLN O_O HR or On SO OY ST NS S oo PLA Ol nr CO CO CO OT ON S CO CO S ST GO CO GO GO lO WO HD e Wry NTN ws rolo nololo Elol nlR ol e O oo sa t SE SU OL s Boe ie BO snd e e so i wlo ol rm ol lolol Nn so co ro OO N oln olajlen ol Alov OT Co D D 7 mi 152 4 148 1 138 1 148 9 151 0 147 5 152 8 159 5 147 5 183 3 168 9 153 1 156 6 i 117 9 2 2 19 9 lt 12 A 19 9 12 m h H 149 4 150
157. effluent water quality and found that the exercises did not influence these two parameters p we Eas man 165 mg L 123 7mg L on average 196mg L 117mg L on average ss 185 mg L 144 2mg L on average 218 mg L 129mg L on average Remark on water quality Total nitrogen 24 mg L 21 2mg L on average 34 mg L 23mg L on average Total phosphorus i 2 8 mg L 2 4mg L on average 4 4 mg L 2 7mg L average 5 4 19 5 mg L 9 9mg L on average 7 5 mg L 2 9mg L on average SS less than 10 mg L less than 10 mg L Total nitrogen 10 16 mg L 13mg L on average 10 14 mg L 12mg L on average 5 C TI rp 802 oC 5 Total phosphorus 1 8mg L 1 3mg L on average 1 8 mg L 1 4mg L on average 1 month Time required for start up 2 1 for installation and 1 month for the whole procedure including trial operation Time Time required for shutdown for shutdown mn min Reliability of the equipment During the verification test the pipes unfastened because they had been temporarily installed in the existent treatment facility but it was repaired immediately There was intended for verification no problem with the body of the equipment How to solve the problems The instruction manual provided information on solving problems Evaluation of the instruction manual of operation and How to solve the problems maintenance equipment was designed in such away that it was in
158. in D cs i f mil oe oe _ ee j 1 i I by i mus i i a E E A Lp Fa ER S en pl O MEMS Beane 9 wee G VERE arenes MAN 9 ere we deo HWE fo ee m m w s Gs S Gs Gs Gs Qs Gss G mm NONM 1 i Ww W EET ma EF FRE m iene EE x Brae H j 4 2 90 43 4 1 4 3 4 1 ET BUCE 15 ere 216 3mm C 1488mm 117kg 25 kg ees F 70 91 90
159. pi _1 j Sn OO ON ol l elo tS Ale rS tS O h N N ON ES ER AN N GOO OTM oO PR das Dl oOo O Pe RB ERS RS OD P EE Ne 8 lo oo la St sS ol OT E N N ow Ron oo a elal ols UO NIU OS eA olo H ol c rs a gt 156 4 163 5 157 1 20 114 H19 11 1 H19 11 2 H19 11 3 H19 11 4 H19 11 5 H19 11 6 H19 11 7 H19 11 8 H19 11 9 H19 11 10 6 00 18 00 w 18 00 H 6 00 n H 0 0 1 5 0 0 1 0 0 0 6 5 0 00 6 4 4 8 6 2 4 9 6 2 4 4 5 6 1 1 00 4 4 4 2 4 2 3 1 2
160. 0 5 8 I 1 0 4 8 12 16 20 J 6 6 7 9 11 19 21 23 05 05 05 x TT RER R Me RT 0 6 12 18 1 2 Alf 912 16 3 3 11 N l I HH iO At 1 A s 7 gt SS H 7X AIS A gt A VER BC J SS SS gt 4 1 iE H H 20 9 18 20 12 4 3 4 1 A
161. 002 81 21 1002 9 1 100 62 11 1002 0 11 100 91 11 1002 8 11 100 1 11 100 92 01 1002 81 01 1002 11 01 1002 01 00Z 10 6 1002 02 6 1002 El 6 700Z 9 6 700Z pH 1 J H 9 2 1 109 pH cm 32 31 30 29 28 27 26 25 24 23 82 8 8002 12 8 8002 8 800Z 7 8 800Z IE 7 800Z 6 800Z 71 800Z 01 800Z 800Z 92 9 8002 61 9 8002 1 9 800 9 9 8005 62 S 8002 6 6 8006 1 G 800Z 8 9 8007 1 800Z yv v 800 L1 v 800 01 800 v 8002 12 8 8002 02 8002 1 800 9 8002 82 2 8002 12 2 8000 bl 800 L 800 IE 1 800Z 6 1 800Z 71 1 800Z 01 1 8002 1 8002 12 01 1002 0 1 100 61 1 1000 9 61 00Z 62 11 1002 20 11 1002 91 11 00 8 11 00 1 11 100 92 01 1002 81 01 00 11 01 1200 1 01 700Z 12 6 1002 02 6 L002 1 6 00Z 9 6 700Z pH 31 HEA V 30 We 2 am J H 2 2 110 250 200 150 F 100 F 50 F 7 1 175 7m i ef fe
162. 04 41 1002 1 61 700Z 9 61 00Z 62 11 1002 0 11 100 91 11 00 8 11 00 1111 1002 9 01 100 81 01 1200 11 01 1002 7 01 00 12 6 1002 02 6 L002 1 6 L002 9 6 L002 pH pH 2 cm 7 04 pH 82 8 8002 12 8 8002 t 1 8 8007 L 8 800 LE 800Z 6 800Z 71 800Z 01 800Z 800Z 92 9 8002 61 9 8002 71 9 8002 G 9 8006 62 8 8007 G 800 91 9 800 8 S 8002 1 9 8007 6 800Z 71 800Z 01 800 800 76 E 800Z 02 8002 1 8002 9 g 800Z 82 2 8006 12 2 8002 Y 1 72 8007 7 Z 800Z LE 1 800Z 6 1 800Z 71 1 800Z 01 1 800 1 8007 12 1 1002 00 21 1002 81 21 1002 9 1 100 62 11 1002 0 11 100 91 11 00 8 11 100 1 11 100 92 01 1002 81 01 1200 11 01 1002 01 100 12 6 1002 02 6 1002 1 6 00Z 9 6 700Z pH 9 pH 7 04 cm 82 8 8002 12 8 8002 t 1 8 8002 7 8 800Z LE 800Z 6 800Z 71 800Z 01 800Z L 8002 92 9 8002 61 9 8002 71 9 8002 G 9 8006 6 G 800 G 800 61 6 8002 8 8 8007 1 9 8007 6 800Z 71 800Z 01 800 800Z 76 E 800Z 02 8002 1 8002 9 g 800Z 86 Z 800Z 12 2 8002 bl 800 L 800 LE 1 800Z 6 1 800Z 71 1 800Z 01 1 800 1 800 12 1 1002 00 21 1
163. 1 6 11 4 CES 12 250 0 170 8m a at a oe 200 0 FE 06 66 61 86 61 46 61 92 01 86 61 1 62 61 66 61 16 1 0G GT 61 1 81 61 41 61 91 61 Sol VI GI ETGT 1 1 11 1 0T T 6 61 8 61 4 1 61 1 9 61 4 9 5T 1 6 1 1 6 GI 1 1 1 RSE I s 5 4 23 m H 173 2m 250 0 200 0 2 184 4 174 4 163 2 170 8 50 0 0 0 9 1 0 1 1 12 EM w 5 5 OO 203 m B i 173 2 m 100 150 200 250 5 6 BU III D ii LLL N
164. 10 NaC10 Na C10 H20 NaC1O Na OH H C10 Na0H HClO 1 HCIO Hcl fo PH 8 9 P C10 HC10 HC10 C10 HC10
165. 10 7 ee 124 10 8 ee 135 10 9 FHA DART cc eee ee ee eee eee cece cece eee nesses 138 10 10 FRYE E ARE 147 10 11 ea 148 2 O SDO A 100 TENA RENE CIO 1
166. 2 6 72 6 32 5 32 5 57 2 S S 6 34 0 4 x 1 2 12 L 5 mg 15
167. 2 149 1 Qo CO J K 7K E H 9 e 10H a 11 12 9 2 4 19 9 12 A 118 19 9 lt 12 A m h 1 T 149 150 2 145 8 re LO 148 0 9 12 153 4 119 lt 19 E 9 12 w 140 8 I 149 4 00 00 00 00 00 00 00 a k ER S JE 1 PH I H 9 2 3 9 12 SS Cle Ce S See a oS ora 206 Seo lun RS ol cq co H i co r ol cq co H Lo cO Moola 40 SK us i wi ih 3 N N 9 2 5 98
168. 2 9 2 9 8 5 15 00 3 0 4 3 4 4 4 5 4 6 4 4 9 2 8 4 5 2 6 16 00 4 4 4 5 5 9 2 8 4 3 4 5 5 4 4 2 8 2 4 17 00 4 5 5 6 5 1 4 1 3 1 4 6 2 4 2 4 4 5 1 18 00 4 8 6 3 8 5 5 6 4 8 6 9 6 3 8 2 9 6 19 00 6 7 7 1 8 6 7 2 6 1 T 6 4 6 6 6 5 12 4 20 00 6 7 7 6 8 7 8 1 6 7 7 1 6 6 8 1 8 7 21 00 6 5 6 5 7 6 9 6 8 1 9 9 2 8 5 8 9 22 00 8 6 8 5 8 4 8 7 8 7 8 9 9 7 9 6 2 23 00 6 9 6 3 0 7 0 T 8 8 6 1 4 H19 12 11 H19 12 12 H19 12 13 H19 12 14 H19 12 15 H19 12 16 H19 12 17 H19 12 18 H19 12 19 H19 12 20 6 00 18 00 ERR HH E s 18 00 22 H 6 00 FE m 0 0 1 0 10 5 0 0 1 0 0 00 3 9 5 0 8 6 2 7 1 6 1 1 00 1 2 5 8 5 4 5 4 4 4 2 2 00 0 1 1 4 6 1 4 1 4 1 3 3 00 0 0 2 3 5 2 4 3 7 29 4 00 0 0 1 9 3 1 3 1 5 1 4 5 00 0 0 1 3 6 2 7 2 3 1 3 6 00 1 3 2 8 9 2 8 2 9 2 9 7 00 4 12 6 6 11 8 15 2 128 8 00 0 14 3 5 15 4 14 9 10 9 9 00 6 11 6 2 11 3 11 9 12 3 10 00 29 9 2 4 8 4 8 7 10 4 8 2 11 00 1 4 4 9 6 1 6 2 6 9 13 4 12 00 5 4 2 4 5 9 6 1 6 9 10 6 13 00 1 6 3 6 6 2 7 0 6 5 6 3 14 00 3 2 7 27 8 0 6 3 4 3 7 6 15 00 4 6 1 8 6 4 2 8 2 7 4 8 16 00 2 4 1 7 4 1 4 2 4 2 5 2 17 00 1 4 5 2 4 3 4 3 5 0 4 2 18 00 0 7 5 7
169. 20 1 0 5 0 05 m e 0 3 mH 6 12 18 hilo RB 2 1 4 50m h 8 1 0 5 18h W154 5 21555 7 29 2 5520 1191 a HCR 16 m ZIT oT 1 4m 2008 4 15 2008 5 20 2008 6 24 86 6 22 H EAE E P 23 22 21 20 19 18 17 16 15 14 13 12 11 10 9 8 7 6 5 4 3 2 1 0 1 0 5 1 1 6 gt 0 6 12 18 2 1
170. 3mm 1 888 mm Body length 1 488 mm Size weight 117 kg including 25 kg for ceramic fill Necessity for pre treatment and No post treatment Supplementary facility Submerged pump chlorine drip strainer control board Life of the equipment Oa os 20 years intended for verification 1 month Time for initiation 2 days for installation and 1 month for the whole procedure including trial operation Installation expense RW 1 set 200 000 Approximate cost including trial operation se transportation expense a ss Other consumption articles 3 000 yen month 3 cans 9 000 sodium hypochlorite 1 m3 of treated wastewater with the condition that the inflow is 270 m3 day The disposal cost of sludge is not included Approximately 7 oOther information from the manufacturer Mecha cera device cuts down the running cost and maintenance fee The device offers a technology that is adaptable to the wastewater treatment facility Type HES is capable of purifying the air of sewage treatment facilities drainage treatment facilities for agricultural use food factories and large ironworks resolving organic solvents for NOx and SOx removal equipment spent hydrochloric acid and sulfuric acid neutralization process equipment at plating factories and titanium oxide air cleaner and deodorizing or oxidatively resolving eight malodorous substances such as toluene xylem hydrogen sulfid
171. 9001 QMS OFA gerys 2007 10 23 2 REARS 148 20 11 11 1703 No 2008 11 19 F amp F kK F s MIAP 7925
172. E BBO HR ce ERN SS 59 5 Bes ithe rath Ra agin 59 5 2 2 ibe See Er Fill Eu HH ate ae 59 5 9 RS q Ea pq 59 5 4 ee ee ee 60 5 5 ER gre we ae 60 5 6 x JJ 61 Dy a Z pla sar Galea ap sul 61 6 62 6 2 R Or er 63 2 T des K IA OI sS 63 3 Soe ak CC a ea S s 63 63 CU RO 64 6 65 6 3 ET ee er ee ee ree 66 67 67 54 1 1 8 1 6 0 0 AO TANE AIP CT WU Du ERO k iS Dod AD ev e
173. E DIE ROA RR ORES PICKLES 5 3 1 OFF 2 3 4 15 5 6 5 ON 5 4 5 5 6
174. O CO OOOH ODM HR UM CO OO IN MIO C CO O O CO OO COCO O O C O O O U CO O O CO I O O NE 11 20 CO H FR WP NO TO OO OO DO O OO OO DO OINI OO UO O OD OI e amp 128 3 1 ES ORT 1 2 55 Rake 3 55 F 1 55 F zk 5 2 55 F zk 5 3 55 Fk 1 2 PHR 3 1 55 2 55 Fak 3 55 F zk 5 1 55 FK 2 55 FK 3 55 1 2 3 1 55 FK 2 55 FK 3 1 2 95 Be BL 3 Be bt 1
175. OI MOT OI SOT MOT OT MOT OT MOT OI MOT OT OI SOT IV 0 8 T 9 MOT OT SOT 9 RSE OT SOT 8 8 MOT OT OT 9 8 OT MOT C 9 hG MOT MOT MOT 8T 8 8 RSE OT SOI E01 MOT E01 v s I P Y OT MOT MOT SOT MOT mO WOT MOT BSE OT MOT MOT 0 9 6 MOT MOT mO MOI SOT 6 8 MOT MOT MOT 8 6 MOT SOT 0 8 Tv BSE OT OI OT MOT OT OT 1 3 H 0G HTT H 8T AIT HOTA IT HST EIT 00 91 eel XE 51215 FRERE HEC Bd H el B 5 20 9
176. S OD JRA A 15 Ve RT fE HEEE SSSI 0 2 2 1 20 11 15 21 5 3 162 9 mi 169 0 m 11 17 152 4 ni 11 21 m H 250 0 p 162 9mY 200 0 gt 100 0 163 6 161 5 169 0 160 3 164 9 168 5 152 4 NN NN KN LN SN NN ss k p k 1 p N k am N m 16 H 11H 17H 114 184A 114 19 EM 5 3 20 11 15 21 H 3 5 4 5 5 5 6
177. TT 7 ONO N G OOV SS i H 105 N
178. amp F kK F MDs 170025 CHIR ZF E 1 1 A AAI Soe N 2009 2 2 i Ls APTS as T oD ie ee
179. e and ammonia The device can be installed in facilities that treat more than 5 m3 of wastewater in day This technology can be use irrespective of the amount of influent water ODS exercises an effect on treating wastewater from the food factories and kitchens as well as oily wastewater from car factories Therefore it reduces waste and cuts down the running cost and maintenance fee to a large extent Outline 4 1 20 6 13 1
180. e Vie AR TARTUK E KET o RE SRE ARE 2 BOD SS P N
181. introduction of the device Asa result from July to September 2008 the amount of sludge was 3 7 m per month and volume loss rate of sludge 75 From October to November 2008 the amount of sludge was 7 4 m3 per month and volume loss rate of sludge 50 The five month average for the amount of sludge was 5 18 m per month and volume loss rate 65 Amount of sludge and volume loss rate of sludge before and after the introduction of the verification device Month when sludge was carried out June 2008 July 2008 August 2008 September 2008 Octorber 2008 Novenber 2008 Verege from July to November 2008 Mecha cera device before the device K after the device was introduced was introduced 14 8 Amount of sludge m 3 7 3 7 3 7 7 4 7 4 Volume loss rate of sludge 75 0 75 0 50 0 50 0 After determining the amount of SS contained in the sludge we calculated the total amount of SS before and after the introduction of the device in order to further examine the components of the volume loss In June 2008 when the device had not been introduced the total amount of SS contained in the sludge was 414 40 kg Meanwhile from July to September 2008 the total amount of SS was 113 59 kg per month and volume loss rate of SS 72 6 From October to November 2008 the total amount of SS was 279 72 kg per month and volume loss rate of SS 32 5 The five month average for the amount of SS was 177 42 kg per month and volume loss rate
182. mg 2 1 16m 20 4 24 H 21 9 4 83 3 4 20 5 1 FEHR 23 1 p 3 1 KARAM AsO Ace k 84 2 3 2 r x i Fe 1 Ho H fk jJ 1 ge RE 2 1 i Ho 4 D gt W gt I 2 ko gt H E RR KR E 7 7
183. of SS 57 2 Formula Total amount of SS kg SS contained in sludge mg L x amount of sludge m3 Total amount of SS contained in sludge and volume loss rate of SS Month when sludge was carried out June 2008 July 2008 August 2008 September 2008 Octorber 2008 Novenber 2008 November 2008 Mecha cera device before the device after the device was introduced ile ES was introduced U SS of sludge mg L 28 000 Amount of sludge m Total amount of SS kg Volume loss rate of SS Taking the above into consideration it is assumed that both the amount of sludge and total amount of SS were reduced by 60 per month during the verification period Outline 2 SEISUI Corp mecha cera device oKnvironmental impact Noise Treatment facilities and neighboring areas 53 dB oUsed resources Amount of electric energy 5 7 kWh day Amount of chemical used for wastewater treatment Sodium hypochlorite 20 kg 3 months oOperation and maintenance of the performance item Maintenance time per operation Number of persons and skills required for Maintenance item and maintenance frequency maintenance we 2 persons knowledge on operation and Periodic check 2 h once a week maintenance 5 1 person knowledge on operation and Cleaning of mecha cera ball 1 day once in six months maintenance oQualitative remark We observed the influence of mecha cera water exercises on the processing unit and
184. stalled on the ground making it easy to fit it within limited space In addition it can be installed either indoors or outdoors depending on the conditions of the facility and almost all the operations are carried out automatically It is necessary to find out a structural way to prevent the sludge from accumulating in the tank after it has been effectively exposed to the mecha cera water Gases It is necessary to find out a way to supply mecha cera water depending on the amount of influent wastewater Since the equipment intended for verification is capable of operating depending on the type and the amount of influent water at each facility it can be installed not only at wastewater treatment facilities for agricultural use but also at facilities that adopt other ways of purification Volume loss of sludge decreases the amount of sludge by 60 per month thereby ensuring that this procedure is cost effective Outline 3 SEISUI Corp mecha cera device Reference information otice The information on this page is supplied by a environmental technology developer who is responsible for the technical bulletin and it is an exception to the verification oProduct data Blank for environmental technology developer Name type Mech cera device SDO A 100 Manufacturer Distributor TEL FAX TEL 022 292 5595 FAX 022 292 5598 SEISUI Corp Contact Web address http www seisul jp address E mail sendai seisul jp 216
185. tees ON RC CS eee eee 5 3 5 4 5 5 6 are eee ee ae ee ee ee ae 7 So Fa ee DSSS 9 cette eee 1 SDO 50 10 eeeeeeeececeeececrecococececececoooooeecececsecoceeee 69 10 1 69 10 2 eae 74 10 3 Dee ee eee cece ee eee eee ween 75 10 4 76 10 5 ARERR R Eee cee eee ee eee eee 10 6 1 121 2 129 3 SS te 123
186. to each tank sodium sludge pooling section Functional ceramic bal filling basket hypochlorite Mecha cera ball Principle Air agitation triggers a catalytic reaction after sodium hypochlorite is added and water or mecha cera water that touches the ceramic in the system is injected into the treatment plant Mecha cera water with sufficient oxidizing capability resolves the organic substance in wastewater or sludge into carbon dioxide H2O water and nitrogen and is effective for reducing the volume of the sludge 2 Outline of the verification experiment oOuthne of the experimental site JARUS III Planned number of men involved in the treatment 700 Planned sewage quantity 189 m day Hourly maximum 22 8 m3 h Quality of influent BOD 200 mg L Quality of treated water BOD 20 mg L Project scale planned value Quantity of Quantity of water to be treated actual quantity of the Ave 173 2m3 day eawacea that eamec in wastewater during experimental verification 100 250 m3 day oSpecifications and performance of the equipment to be verified Outline of the facility 216 3 mm w x 1 888 mm body length 1 488 mm Size Weight 117 kg Gncluding 25 kg for ceramic fill ae Maximum 270 m day i iti mount of wastewater per da 4 adjustable to 50 m3 day Treatment object Volume loss of sludge by more than 70
187. x HH J 27 2 x A 1 2 3 1 2 lt I pave Crim 5 5 gt x He eeeeeeeeeeeeeeeeeeeeeeee Ka wi 5y Hy rN 1 9 3 2 85 3 5 3 3 3 3 Gil H 11 7m h 24 2 ARE XK HES j Khi 1S 6 BZ 7 9 11 19 21 23 2 1 6 1 0 6m H7 2m 0 2 2 1 were 6 0 4 8 12 16

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