KR950003192A - Manure Advanced Treatment - Google Patents

Manure Advanced Treatment Download PDF

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Publication number
KR950003192A
KR950003192A KR1019930014379A KR930014379A KR950003192A KR 950003192 A KR950003192 A KR 950003192A KR 1019930014379 A KR1019930014379 A KR 1019930014379A KR 930014379 A KR930014379 A KR 930014379A KR 950003192 A KR950003192 A KR 950003192A
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KR
South Korea
Prior art keywords
manure
centrifuge
sewage
treatment
distillation chamber
Prior art date
Application number
KR1019930014379A
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Korean (ko)
Other versions
KR0169304B1 (en
Inventor
김재우
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김재우
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Application filed by 김재우 filed Critical 김재우
Priority to KR1019930014379A priority Critical patent/KR0169304B1/en
Publication of KR950003192A publication Critical patent/KR950003192A/en
Application granted granted Critical
Publication of KR0169304B1 publication Critical patent/KR0169304B1/en

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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/123Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using belt or band filters
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/02Biological treatment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00Treatment of sludge; Devices therefor
    • C02F11/12Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/005Black water originating from toilets

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  • Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Molecular Biology (AREA)
  • Treatment Of Sludge (AREA)
  • Fertilizers (AREA)

Abstract

본 발명은 분뇨에 함유된 총량 고형물을 원심분리기를 이용하여 초기공정에서 완벽하게 제거하고, 분과뇨만을 하수와 병합처리하거나 청등수를 생산하는 공정을 거쳐 방류수 없이 소미립자로 대기화 시키는 분뇨고도처리방법에 관한 것이다. 즉, 분뇨의 성상과 환경조건 변화에 구애받지 않고 기존 처리방법과 시설을 배제하고 하수와 병합처리코져 할때에는 분뇨에 함유된 총량 고형물을 원심분리기(6)으로 초기공정에서 완벽하게 제거하여 분과 뇨만을 하수처리공정과 연계하여 처리토록하며 ; 분뇨 치리시설을 단독으로 운영코져 할때는 상기 원심분리기(6)를 거친 분과 뇨를 저류소화조(7), 탈수기(10)등을 거치면서 생산된 청등수를 건류실(35)와 증발실(37)로 대분된 기화조(12)를 통하여 방류수없이 소미립자로 기화시키는 특징을 갖는다.The present invention completely removes the total amount of solids contained in the manure in the initial process using a centrifugal separator, and the manure-altitude treatment to make the manure into atmospheric air with small particles without effluent through the process of combining only manure with sewage or producing blue water. It is about a method. In other words, regardless of the characteristics of manure and changes in environmental conditions, when the existing treatment methods and facilities are excluded and combined treatment with sewage, the total amount of solids contained in the manure is completely removed in the initial process by the centrifuge (6). To treat the bay in conjunction with sewage treatment; When the manure control facility is operated independently, the fresh water produced through the centrifuge (6) and the urine storage tank (7), the dehydrator (10), etc. It is characterized by vaporizing into small particles without effluent through the vaporization tank 12 divided into.

Description

분뇨 고도처리방법Manure Advanced Treatment

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

Claims (2)

벨트스크린 협잡물처리기(2)에서 협잡물이 제거된 분리액을 원심분리기(6)의해 함수율 75%이하로 탈수하는 분뇨 고도고액 원심분리식 처리방법의 전처리 공정에 있어서; 원심 분리기(6)에서 탈수된 고형물을 회수하여 발효조(13)에서 발효시켜 유기질 퇴비로 사용케하며; 원심분리기에서 분리된 분리액을 하수 처리장의 침전조에 유입시켜 하수와 병합처리토록 한것을 특징으로하는 분뇨 고도처리방법.In the pretreatment process of the high-density solid-liquid centrifugal treatment method of dewatering the separation liquid from which the contaminant was removed by the belt screen contaminant processing machine to below 75% of water content by the centrifuge 6; Recovering the solid dehydrated in the centrifuge (6) and fermented in the fermenter (13) for use as organic compost; A high manure treatment method characterized in that the separated liquid separated in the centrifuge flows into the sedimentation tank of the sewage treatment plant to be combined with sewage. 원심분리기(6)에서 분리된 분리액에 함유된 소화되지않은 분과점성을 저류소화조(7)에서 소화를 거치고 약픔혼화조(8)에서 염화 제2철로 산화하여 고분자응집제로 미세미립자를 Floc화합하여 탈수기(10)에서 고액분리하고, 분이제거된 뇨를 원심여과기(11)를 거쳐 잔류고분자 응집제나 잔류 부유물을 제거한 청등수를; 기화조(12)의 건류실(35)에 내장된 열교환코일(36)에 고압펌프로 유입시켜 예비가열케하여 증발로(37)의 외부 일단면에 장설된 다수개의 노즐(38)로 증발로(37)내부 상단에 미세하게 분무하고, 증발로(37)의 집수조(39)에 집수되는 뇨는 집수조(39)와 연결된 고압펌프로 외부 다른 단면 노즐(38')로 증발로(37)내부에 분무하고, 집수된 뇨를 방열판넬(40)에 의해 증발되는 증기와 화합한 농무를 진공펌프로 건류실(35)에 인입시키고 고열열풍기(42)로 400로씨 이상의 고열열풍을 건류실(35)에 유입시켜 농무와 혼합케하여 저밀도충진망(43)을 통과케하여 농무를 초미립자로 분해키고, 열교환 코일(36)과 고밀도충진망(44)를 통과하면서 소미립자로 분해되고 유해가스는 Bio Dash(45)를 통과시켜 제거하고 순수 수분만을 소미립자로 대리에 혼화시키는 것을 특징으로 하는 분뇨 고도 처리방법.The undigested branch viscosity contained in the separation liquid separated by the centrifuge (6) was digested in the storage digestion tank (7) and oxidized to ferric chloride in the weak mixture (8) to flocculate fine particles into a polymer coagulant. Solid-liquid separation in the dehydrator (10) and the demineralized urine to remove the residual polymer flocculant or residual suspended solids through a centrifugal filter (11); A high pressure pump flows into the heat exchange coil 36 embedded in the distillation chamber 35 of the vaporization tank 12 to preheat it, and then to the evaporation furnace with a plurality of nozzles 38 installed on one end surface of the evaporation furnace 37. (37) finely sprayed on the upper end, the urine collected in the sump (39) of the evaporation furnace 37 is a high-pressure pump connected to the sump (39) inside the evaporator (37) to the other end face nozzle 38 ' Spray the collected urine into the distillation chamber (35) with a vapor pumped by the heat dissipation panel (40) into the distillation chamber (35), and the high-temperature hot air (42) with high-temperature hot air of 400 ° C or more in the distillation chamber (35). ) And mixed with agricultural soils to pass through the low density filling network (43) to decompose the agricultural particles into ultra-fine particles, and breaks down into small particles while passing through the heat exchange coil (36) and the high density filling network (44). Removed by passing through the Dash (45) and the manure, characterized in that only the pure water is mixed in small particles fine Advanced treatment. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019930014379A 1993-07-26 1993-07-26 Animal waste disposal process KR0169304B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1019930014379A KR0169304B1 (en) 1993-07-26 1993-07-26 Animal waste disposal process

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1019930014379A KR0169304B1 (en) 1993-07-26 1993-07-26 Animal waste disposal process

Publications (2)

Publication Number Publication Date
KR950003192A true KR950003192A (en) 1995-02-16
KR0169304B1 KR0169304B1 (en) 1999-01-15

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KR1019930014379A KR0169304B1 (en) 1993-07-26 1993-07-26 Animal waste disposal process

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100311758B1 (en) * 1999-05-13 2001-11-14 구본탁 Bioconversion apparatus and process of the various high-concentrated organic waste using semi-continuous liquid fermentation

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100340191B1 (en) * 1999-04-29 2002-06-12 김재우 Food waste recycling apparatus
KR100723338B1 (en) * 2006-11-17 2007-05-30 백구엔지니어링(주) Recycling disposal plant system for livestock excretions
CN103951148B (en) * 2014-04-23 2016-05-04 江苏康泰环保设备有限公司 A kind of plant's ight soil utilization system and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100311758B1 (en) * 1999-05-13 2001-11-14 구본탁 Bioconversion apparatus and process of the various high-concentrated organic waste using semi-continuous liquid fermentation

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