KR20030001698A - Waste water processing system of food and drink - Google Patents
Waste water processing system of food and drink Download PDFInfo
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- KR20030001698A KR20030001698A KR1020010036539A KR20010036539A KR20030001698A KR 20030001698 A KR20030001698 A KR 20030001698A KR 1020010036539 A KR1020010036539 A KR 1020010036539A KR 20010036539 A KR20010036539 A KR 20010036539A KR 20030001698 A KR20030001698 A KR 20030001698A
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
본 발명은 수집된 음식물 등의 폐기물에서 발생하는 고농도 폐수를 응집하고 가압, 탈수하여 폐수를 탈리시키고 상기 폐수가 탈리된 음식물 폐기물은 발효를 위한 발효수단으로 이동시키며, 상기 탈리된 폐수는 탈수 및 가압부상시키면서 정화시키도록 하므로써 상기 음식물 폐기물에서 탈리된 탈리액 등의 고농도 폐수를 효율적으로 처리할 수 있도록 한 유지방이 많이 함유된 음식물 쓰레기의 탈리액 및 고농도 폐수처리시스템에 관한 것이다.The present invention aggregates, pressurizes, and dehydrates high-density wastewater generated from wastes such as collected foods to desorb wastewater, and the wastewater is removed from the wastewater to a fermentation means for fermentation, and the dewatered wastewater is dewatered and pressurized. The present invention relates to a degreasing solution and a high concentration wastewater treatment system for a food waste containing a large amount of milk fat which can efficiently treat a high concentration wastewater such as a desorption liquid desorbed from the food waste by allowing it to be purified while floating.
일반적으로 음식물 쓰레기나 각종 폐기물 등은 그 자체를 그대로 폐기할 수 없기 때문에 상기 폐기물들을 분리한 다음, 이를 소각시키거나 재활용이 가능한 폐기물을 분리하여 건조하고 이 건조된 폐기물을 산업상 필요한 자원으로 재활용할 수 있도록 하고 있으며, 특히 상기 음식물 쓰레기 등은 슬럿지상태로 만들어 이를 소각로나 건조로로 보내기 위하여 수집된 음식물 쓰레기를 사일로에 저장하고 있었다.In general, food waste or various wastes cannot be disposed of as they are. Therefore, the wastes can be separated, incinerated or recycled, and the wastes can be dried and recycled as industrial resources. In particular, the food waste was made into a sludge state, and the collected food waste was stored in a silo to be sent to an incinerator or a drying furnace.
또한, 상기 음식물 쓰레기를 처리함에 있어서는 많은 수분이 함유되어 있기 때문에 상기 음식물 쓰레기를 건조하고 소각시키는 방법만으로는 상기 음식물 쓰레기에 함유된 폐수를 모두 증발시키거나 처리할 수 없었으며, 이에 따라 상기 음식물쓰레기에서 발생되는 폐수는 그대로 방출하게 되는 일이 발생되므로써 방출되는 상기 폐수에 의한 수질의 오염을 야기시키게 되는 폐단이 있었다.In addition, since the food waste contains a lot of water, only the method of drying and incinerating the food waste could not evaporate or treat all of the wastewater contained in the food waste, and thus, in the food waste The wastewater generated was discharged as it is, and there was a wastewater that caused pollution of the water by the wastewater discharged.
또, 상기 음식물 쓰레기를 그대로 매립시킬 경우에는 상기 음식물 쓰레기에서 발생되는 폐수가 그대로 지반으로 침투되기 때문에 침출수에 의한 지하수의 오염과 더불어 토지를 오염시키게 되는 점등의 문제점이 있었다.In addition, when the food waste is landfilled as it is, wastewater generated from the food waste is infiltrated into the ground, which causes a problem of lighting that contaminates the land together with groundwater contamination by leachate.
본 발명은 상기와 같은 종래의 제반 문제점을 감안하여 안출한 것으로, 본 발명은 수집된 음식물 등의 폐기물에서 발생하는 고농도 폐수를 응집하고 가압, 탈수하여 폐수를 탈리시키고 상기 폐수가 탈리된 음식물 폐기물은 발효를 위한 발효수단으로 이동시키며, 상기 탈리된 폐수는 탈수 및 가압부상시키면서 정화시키도록 하므로써 상기 음식물 폐기물에서 탈리된 탈리액 등의 고농도 폐수를 효율적으로 처리할 수 있도록 한 유지방이 많이 함유된 음식물 쓰레기의 탈리액 및 고농도 폐수처리시스템을 제공하려는 것인바, 이를 이하에서 첨부한 도면에 의거하여 상세히 설명하면 다음과 같다.The present invention has been made in view of the above-mentioned conventional problems, the present invention is agglomerated and pressurized, dewatered high concentration wastewater generated from the collected waste, such as food wastes to remove the waste water and the food waste from which the waste water is removed By moving to the fermentation means for fermentation, the dewatered wastewater is dehydrated and pressurized to purify the high-density waste foods such as desorption liquor from the food waste, so as to efficiently treat It is intended to provide a desorption liquid and a high concentration wastewater treatment system, which will be described below in detail with reference to the accompanying drawings.
도 1은 본 발명 실시예의 시스템을 나타내는 구성도1 is a block diagram showing a system of an embodiment of the present invention.
<도면의주요부분에대한부호설명><Description of Symbols on Main Parts of Drawing>
1 : 응집탱크1: coagulation tank
2 : 양이온탱크2: cation tank
3 : 음이온탱크3: anion tank
4 : 탈수수단4: dewatering means
5 : 제1처리조5: first treatment tank
6 : 파이프 응집기6: pipe flocculator
7 : 부상분리기7: floating separator
8 : 원수저류조8: raw water storage tank
9 : 2차 저류조9: secondary storage tank
10 : 응집제 용해수단10: flocculant dissolving means
11 : 혼화제 탱크11: Admixture Tank
12 : 중화제탱크12: neutralizing tank
13 : 폐수정화 처리수단13: wastewater purification treatment means
14 : 잉여 슬럿지 반송처리수단14: surplus sludge conveying processing means
15 : 배출부15: discharge part
양, 음이온탱크(2)(3)가 연결된 응집탱크(1)에 탈수수단(4)을 연결설치하고, 이 탈수수단(4)에서 폐기물을 탈수하여 폐수를 탈리시켜 제1처리조(5)로 보내도록 하며, 이 제1처리조(5)로 이송된 폐수는 파이프 응집기(6)를 통하여 부상분리기(7)로 이송시킨다.The dehydration means (4) is connected to the coagulation tank (1) to which the positive and negative ion tanks (2) and (3) are connected, and the dewatering means is dewatered to desorb the waste water to thereby remove the first treatment tank (5). The wastewater transferred to the first treatment tank 5 is transferred to the flotation separator 7 through the pipe flocculator 6.
상기 부상분리기(7)에서는 폐수를 부상작용으로 부상시켜 폐수에 함유된 슬럿지를 분리시키고, 이 부상분리기(7)에서 분리된 슬럿지와 폐수는 각각 원수저류조(8)와 2차 저류조(9)로 보내도록 한다.The flotation separator (7) floats the wastewater by flotation to separate the sludge contained in the wastewater, and the sludge and the wastewater separated from the flotation separator (7) are fed into the raw water storage tank (8) and the secondary storage tank (9), respectively. Send it.
상기 파이프 응집기(6)에는 용수가 공급되는 응집제 용해수단(10)과 혼화제 탱크(11), 중화제 탱크(12)들을 순차적으로 연결시켜 상기 제1처리조(5)로부터 처리되어 부상분리기(7)로 이송되는 폐수는 파이프 응집기(6)에서 응집되도록 하며, 상기 2차 저류조(9)에는 생물학적 처리수단인 폐수정화 처리수단(13)을 연결하여 상기 음식물 쓰레기에서 탈리된 탈리액을 정화시키고 잉여 슬럿지 반송처리수단(14)을 연결하여 효율적인 정화를 촉진시키며 이를 배출부(15)로 배출시킬 수 있도록 구성한 것이다.The pipe flocculator 6 is connected to the flocculant dissolving means 10, the admixture tank 11, and the neutralizer tank 12 to which water is supplied, and is processed from the first treatment tank 5, thereby allowing the flocculator 7 to float. Wastewater transported to the c) is agglomerated in the pipe agglomerator (6), and the secondary storage tank (9) is connected to the wastewater purification treatment means (13), which is a biological treatment means, to purify the desorption liquid removed from the food waste and surplus. By connecting the sludge conveying treatment means 14 is to promote efficient purification and to discharge it to the discharge unit (15).
이하에서 상기와 같이 구성된 본 발명의 작용상태를 설명한다.Hereinafter will be described the working state of the present invention configured as described above.
상기 양, 음이온탱크(2)(3)를 통하여 이온화된 폐기물이 응집탱크(1)에서 응집되면서 상기 탈수수단(4)으로 공급되면, 이 탈수수단(4)에서 상기 폐기물을 가압하여 음식물 쓰레기로부터 폐수를 탈리시키게 되고, 상기 폐수가 탈리된 음식물 쓰레기는 발효동으로 이송된다.When the wastes ionized through the positive and negative ion tanks 2 and 3 are supplied to the dewatering means 4 while being agglomerated in the agglomeration tank 1, the dewatering means 4 pressurizes the wastes from the food waste. The wastewater is desorbed, and the food waste from which the wastewater is desorbed is transferred to the fermentation copper.
상기 탈리된 폐수는 탈수수단(4)에서 제1처리조(5)로 보내도록 하며, 이 제1처리조(5) 1차로 처리된 폐수는 파이프 응집기(6)를 통하여 부상분리기(7)로 이송시키게 되는 데, 상기 파이프 응집기(6)에는 용수가 공급되는 응집제 용해수단(10)과 혼화제 탱크(11), 중화제탱크(12)들이 순차적으로 연결되어 이들로부터 공급되는 처리제와 상기 폐수를 혼합, 응집시키면서 부상분리기(7)로 이송한다.The dewatered wastewater is sent from the dewatering means (4) to the first treatment tank (5), and the first treated wastewater (5) is treated as a flotation separator (7) through a pipe agglomerator (6). In the pipe agglomerate 6, the flocculant dissolving means 10, the admixture tank 11, and the neutralizer tank 12 supplied with water are sequentially connected to the pipe agglomerator 6 to supply the treatment agent and the wastewater supplied therefrom. The mixture is transferred to the flotation separator (7) while mixing and flocculating.
상기 부상분리기(7)에서는 이송되어온 폐수를 부상작용으로 부상시켜 폐수에 함유된 슬럿지를 분리시키고, 이 부상분리기(7)에서 분리된 슬럿지와 폐수는 각각 원수저류조(8)와 2차 저류조(9)로 보내도록 하며, 원수저류조(8)에서는 슬럿지가 함유된 폐수를 다시 상기 응집탱크(1)로 보내어 재처리하도록 하고, 2차 저류조(9)로 보내지는 폐수는 생물학적 처리수단인 폐수정화 처리수단(13)으로 이송시키며 이 폐수정화 처리수단(13)을 통하여 상기 음식물 쓰레기에서 탈리된 탈리액 및 고농도 폐수를 정화시키면서 이를 배출부(15)로 배출시킬 수 있도록 하고, 상기 정화작용 후의 잉여 슬럿지는 잉여 슬럿지 반송처리수단(14)을 통하여 반송처리하도록 한 것이다.In the flotation separator (7), the transported wastewater is floated by flotation to separate sludge contained in the wastewater, and the sludge and wastewater separated in the flotation separator (7) are respectively stored in the raw water storage tank (8) and the secondary storage tank (9). In the raw water storage tank (8), the wastewater containing sludge is sent back to the flocculation tank (1) for reprocessing, and the wastewater sent to the secondary storage tank (9) is a wastewater purification treatment which is a biological treatment means. The waste water purifying means 13 is transferred to the means 13 to purify the desorption liquid and the high concentration wastewater desorbed from the food waste, and to discharge it to the discharge part 15, and the excess sludge after the purifying action The surplus sludge conveyance processing means 14 is used for conveyance processing.
이상과 같은 본 발명은 상기와 같이 음식물 쓰레기에 함유된 수분등의 폐수를 응집, 가압, 부상작용 및 생물학적 처리 등으로 폐기물과 폐수를 분리시키고 상기 분리되어 탈리되는 폐수를 정화처리하여 정수되도록 하며, 상기 수분이 탈리된 음식물 쓰레기는 발효를 시킬 수 있도록 하여 이를 재활용하도록 하므로써 상기 음식물 쓰레기에 의한 환경오염을 방지할 수 있게 되고, 상기 폐수를 정화시켜 배출하도록 하므로써 종래와 같이 음식물 쓰레기의 침출수가 그대로 지반으로 침투되어 지하수나 상하수도 및 토지가 오염되는 것을 방지할 수 있게 되는 점등의 특징을 지닌 것이다.As described above, the present invention separates waste and wastewater by agglomeration, pressurization, flotation and biological treatment of wastewater such as moisture contained in food waste as described above, and purifies the wastewater to be separated and desorbed to purify. The food waste from which the water has been removed can be fermented to be recycled, thereby preventing environmental pollution caused by the food waste, and by clarifying and discharging the waste water, the leachate of the food waste remains as it is. It has a characteristic of lighting that can be prevented from being contaminated and contaminated groundwater, water and sewage, and land.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100521649B1 (en) * | 2003-09-24 | 2005-10-13 | 손을택 | Small sewage terminal treatment method |
CN104045211A (en) * | 2014-06-24 | 2014-09-17 | 芜湖富春染织有限公司 | Reclaimed water reuse system in deep printing and dyeing wastewater treatment |
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JPH06226290A (en) * | 1993-02-05 | 1994-08-16 | Kurita Water Ind Ltd | Treatment of night soil and septic tank sludge |
JPH0919700A (en) * | 1995-07-04 | 1997-01-21 | Sumitomo Heavy Ind Ltd | Sewage treating device |
KR970059118A (en) * | 1996-01-31 | 1997-08-12 | 박형인 | How to purify organic wastewater |
KR20010009316A (en) * | 1999-07-05 | 2001-02-05 | 황경욱 | Pig excretion disposal device |
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2001
- 2001-06-26 KR KR1020010036539A patent/KR20030001698A/en not_active Application Discontinuation
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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JPH06226290A (en) * | 1993-02-05 | 1994-08-16 | Kurita Water Ind Ltd | Treatment of night soil and septic tank sludge |
JPH0919700A (en) * | 1995-07-04 | 1997-01-21 | Sumitomo Heavy Ind Ltd | Sewage treating device |
KR970059118A (en) * | 1996-01-31 | 1997-08-12 | 박형인 | How to purify organic wastewater |
KR20010009316A (en) * | 1999-07-05 | 2001-02-05 | 황경욱 | Pig excretion disposal device |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100521649B1 (en) * | 2003-09-24 | 2005-10-13 | 손을택 | Small sewage terminal treatment method |
CN104045211A (en) * | 2014-06-24 | 2014-09-17 | 芜湖富春染织有限公司 | Reclaimed water reuse system in deep printing and dyeing wastewater treatment |
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