METHOD AND APPARATUS FOR COOLING EFFLUENT NEUTRALISE SYSTEM (CENS)
THERE IS PROVIDED A METHOD (18) FOR COOLING EFFLUENT NEUTRALISATION SYSTEM, THE METHOD (18) COMPRISING: DIRECTLY FEEDING MIXTURE OF OIL, SLUDGE, AND WATER INTO A DE-OILING TANK (6) THAT BREAKUP THE OIL, SLUDGE, AND WATER; AND DISCHARGING TO A COOLING TANK (7) TO BRING DOWN THE TEMPERATURE FOR ANAERO...
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| creator | IR. NG CHENG SINN LOI SWING YEW |
| description | THERE IS PROVIDED A METHOD (18) FOR COOLING EFFLUENT NEUTRALISATION SYSTEM, THE METHOD (18) COMPRISING: DIRECTLY FEEDING MIXTURE OF OIL, SLUDGE, AND WATER INTO A DE-OILING TANK (6) THAT BREAKUP THE OIL, SLUDGE, AND WATER; AND DISCHARGING TO A COOLING TANK (7) TO BRING DOWN THE TEMPERATURE FOR ANAEROBIC PROCESS TO TAKE PLACE. FROM THE COOLING TANK (7) AFTER OBTAINING THE PRE-REQUISITE TEMPERATURE, THE MIXTURE WILL BE SEND TO THE ANAEROBIC TANK (8) TO FURTHER HOMOGENEOUS THE MIXTURE USING STIRRER (9).THE MIXTURE FROM THE ANAEROBIC TANK (8) WILL BE SEND TO THE INTERMEDIATE BIO-GAS TANKS (10), TO FURTHER RELEASE THE GASEOUS TO THE ATMOSPHERE AND LEAVING THE LIQUID TO BE OVERFLOW TO THE MEDIA TANKS ( 12 ) FOR AEROBIC PROCESS TO TAKE PLACE.THE COMPRESSOR (11) PUMPING AIR USE TO FACILITATE THE AMOUNT OF OXYGEN BY INTRODUCES TO THE MEDIA TANKS (12) FOR AEROBIC PROCESS TO TAKE PLACE.THE LIQUID FROM THE MEDIA TANKS (12) WILL GO THROUGH FILTER (13) TO ABSORB THE ODOUR AND SUBSTANCES WHICH STILL REMAIN INSIDE THE LIQUID.THE FINAL LIQUID DISCHARGE FROM THE FILTER WILL ENTER AN IRRIGATION POND (14).THE SOLID BED (15) FUNCTION IS TO COLLECT THE SEMI SOLID FROM THE DE-OILING TANK (6), ANAEROBIC TANKS (8), AND INTERMEDIATE BIO-GAS TANKS (10) |
| format | Patent |
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NG CHENG SINN ; LOI SWING YEW</creatorcontrib><description>THERE IS PROVIDED A METHOD (18) FOR COOLING EFFLUENT NEUTRALISATION SYSTEM, THE METHOD (18) COMPRISING: DIRECTLY FEEDING MIXTURE OF OIL, SLUDGE, AND WATER INTO A DE-OILING TANK (6) THAT BREAKUP THE OIL, SLUDGE, AND WATER; AND DISCHARGING TO A COOLING TANK (7) TO BRING DOWN THE TEMPERATURE FOR ANAEROBIC PROCESS TO TAKE PLACE. FROM THE COOLING TANK (7) AFTER OBTAINING THE PRE-REQUISITE TEMPERATURE, THE MIXTURE WILL BE SEND TO THE ANAEROBIC TANK (8) TO FURTHER HOMOGENEOUS THE MIXTURE USING STIRRER (9).THE MIXTURE FROM THE ANAEROBIC TANK (8) WILL BE SEND TO THE INTERMEDIATE BIO-GAS TANKS (10), TO FURTHER RELEASE THE GASEOUS TO THE ATMOSPHERE AND LEAVING THE LIQUID TO BE OVERFLOW TO THE MEDIA TANKS ( 12 ) FOR AEROBIC PROCESS TO TAKE PLACE.THE COMPRESSOR (11) PUMPING AIR USE TO FACILITATE THE AMOUNT OF OXYGEN BY INTRODUCES TO THE MEDIA TANKS (12) FOR AEROBIC PROCESS TO TAKE PLACE.THE LIQUID FROM THE MEDIA TANKS (12) WILL GO THROUGH FILTER (13) TO ABSORB THE ODOUR AND SUBSTANCES WHICH STILL REMAIN INSIDE THE LIQUID.THE FINAL LIQUID DISCHARGE FROM THE FILTER WILL ENTER AN IRRIGATION POND (14).THE SOLID BED (15) FUNCTION IS TO COLLECT THE SEMI SOLID FROM THE DE-OILING TANK (6), ANAEROBIC TANKS (8), AND INTERMEDIATE BIO-GAS TANKS (10)</description><language>eng</language><subject>CHEMISTRY ; METALLURGY ; TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE</subject><creationdate>2016</creationdate><oa>free_for_read</oa><woscitedreferencessubscribed>false</woscitedreferencessubscribed></display><links><openurl>$$Topenurl_article</openurl><openurlfulltext>$$Topenurlfull_article</openurlfulltext><thumbnail>$$Tsyndetics_thumb_exl</thumbnail><linktohtml>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20161031&DB=EPODOC&CC=MY&NR=158612A$$EHTML$$P50$$Gepo$$Hfree_for_read</linktohtml><link.rule.ids>230,308,776,881,25542,76289</link.rule.ids><linktorsrc>$$Uhttps://worldwide.espacenet.com/publicationDetails/biblio?FT=D&date=20161031&DB=EPODOC&CC=MY&NR=158612A$$EView_record_in_European_Patent_Office$$FView_record_in_$$GEuropean_Patent_Office$$Hfree_for_read</linktorsrc></links><search><creatorcontrib>IR. NG CHENG SINN</creatorcontrib><creatorcontrib>LOI SWING YEW</creatorcontrib><title>METHOD AND APPARATUS FOR COOLING EFFLUENT NEUTRALISE SYSTEM (CENS)</title><description>THERE IS PROVIDED A METHOD (18) FOR COOLING EFFLUENT NEUTRALISATION SYSTEM, THE METHOD (18) COMPRISING: DIRECTLY FEEDING MIXTURE OF OIL, SLUDGE, AND WATER INTO A DE-OILING TANK (6) THAT BREAKUP THE OIL, SLUDGE, AND WATER; AND DISCHARGING TO A COOLING TANK (7) TO BRING DOWN THE TEMPERATURE FOR ANAEROBIC PROCESS TO TAKE PLACE. 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NG CHENG SINN</au><au>LOI SWING YEW</au><format>patent</format><genre>patent</genre><ristype>GEN</ristype><title>METHOD AND APPARATUS FOR COOLING EFFLUENT NEUTRALISE SYSTEM (CENS)</title><date>2016-10-31</date><risdate>2016</risdate><abstract>THERE IS PROVIDED A METHOD (18) FOR COOLING EFFLUENT NEUTRALISATION SYSTEM, THE METHOD (18) COMPRISING: DIRECTLY FEEDING MIXTURE OF OIL, SLUDGE, AND WATER INTO A DE-OILING TANK (6) THAT BREAKUP THE OIL, SLUDGE, AND WATER; AND DISCHARGING TO A COOLING TANK (7) TO BRING DOWN THE TEMPERATURE FOR ANAEROBIC PROCESS TO TAKE PLACE. FROM THE COOLING TANK (7) AFTER OBTAINING THE PRE-REQUISITE TEMPERATURE, THE MIXTURE WILL BE SEND TO THE ANAEROBIC TANK (8) TO FURTHER HOMOGENEOUS THE MIXTURE USING STIRRER (9).THE MIXTURE FROM THE ANAEROBIC TANK (8) WILL BE SEND TO THE INTERMEDIATE BIO-GAS TANKS (10), TO FURTHER RELEASE THE GASEOUS TO THE ATMOSPHERE AND LEAVING THE LIQUID TO BE OVERFLOW TO THE MEDIA TANKS ( 12 ) FOR AEROBIC PROCESS TO TAKE PLACE.THE COMPRESSOR (11) PUMPING AIR USE TO FACILITATE THE AMOUNT OF OXYGEN BY INTRODUCES TO THE MEDIA TANKS (12) FOR AEROBIC PROCESS TO TAKE PLACE.THE LIQUID FROM THE MEDIA TANKS (12) WILL GO THROUGH FILTER (13) TO ABSORB THE ODOUR AND SUBSTANCES WHICH STILL REMAIN INSIDE THE LIQUID.THE FINAL LIQUID DISCHARGE FROM THE FILTER WILL ENTER AN IRRIGATION POND (14).THE SOLID BED (15) FUNCTION IS TO COLLECT THE SEMI SOLID FROM THE DE-OILING TANK (6), ANAEROBIC TANKS (8), AND INTERMEDIATE BIO-GAS TANKS (10)</abstract><oa>free_for_read</oa></addata></record> |
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| subjects | CHEMISTRY METALLURGY TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE |
| title | METHOD AND APPARATUS FOR COOLING EFFLUENT NEUTRALISE SYSTEM (CENS) |
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