KR20050121306A - Food waste water processing apparatus used dissolved air flotation unit and biological chemical reacting - Google Patents
Food waste water processing apparatus used dissolved air flotation unit and biological chemical reacting Download PDFInfo
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Abstract
본 발명은 수집된 음식물 등의 폐기물에서 발생하는 고농도 폐수를 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 폐수처리장치에 관한 것이다.The present invention pressurizes and dewaters high concentration wastewater generated from waste such as collected foods to desorb wastewater, and the wastewater is removed from the wastewater to a fermentation means for fermentation, and the desorbed wastewater is dehydrated and pressurized. The present invention relates to a desorption liquid and a high concentration wastewater treatment apparatus for a food waste containing a large amount of milk fat which can efficiently treat high concentration wastewater such as desorption liquid desorbed from the food waste by purifying.
본 발명은 협잡물제거기(4)에서 탈리된 탈리액을 저류조(9)로 이송시켜 폐수를 파이프 응집기(14)를 통하여 가압부상분리기(15)로 이송시키고, 상기 가압부상분리기(15)에서는 폐수를 부상작용으로 부상시켜 폐수에 함유된 슬러지를 분리시켜, 이 가압부상분리기(15)에서 분리된 슬럿지와 폐수는 각각 슬럿지 저류조(33)와 생화학 반응조(21)로 보내며, 상기 파이프 응집기(14)에는 용수가 공급되는 응집제 용해수단(11-1)과 혼화제 탱크(11-2), 중화제 탱크(11-3)들을 순차적으로 연결시키고 상기 저류조(9)로부터 처리되어 가압부상분리기(15)로 이송되는 폐수는 파이프 응집기(14)에서 응집되도록 하며, 생화학 반응조(21)에는 폐수정화수단인 침전조(36)에서 안정적인 침전을 유도하기 위해 생화학반응조(21)에서 산화약품을 첨가하여 일정온도를 유지하면서 체류시킨 다음 미생물조(25), MSR반응조(30), 전기화학 반응기(32)를 거쳐 침전조(36)로 이송된다. 침전조(36)에서 침전된 상등수는 맑은물이 되어 배출되며, 이때 발생되는 침전 슬럿지는 가압부상분리기(15)에서 발생된 슬럿지와 저장혼합(33)해서 탈수 수단인 탈수기(38)로 탈수하여 고형물질을 분리 배출한다.The present invention transfers the desorption liquid desorbed from the contaminant remover (4) to the storage tank (9) to transfer the wastewater to the pressure flotation separator (15) through the pipe flocculator (14), and in the pressurized flotation separator (15). The sludge contained in the wastewater by flotation by flotation is separated, and the sludge and the wastewater separated by the pressure float separator 15 are sent to the sludge storage tank 33 and the biochemical reaction tank 21, respectively, and the pipe agglomerate 14 The flocculant dissolving means (11-1), admixture tank (11-2), neutralizer tank (11-3) is supplied to the water in sequence and is processed from the storage tank (9) is transferred to the pressure flotation separator (15) The waste water to be agglomerated in the pipe agglomerator 14, the biochemical reaction tank 21 to maintain a constant temperature by adding an oxidizing agent in the biochemical reaction tank 21 to induce a stable precipitation in the sedimentation tank 36, which is a waste water purification means While staying Then it is sent to the microbiology (25), MSR reaction tank 30, a settling tank 36 through the electrochemical reactor (32). The supernatant precipitated in the sedimentation tank 36 is discharged as clear water, and the sediment sludge generated at this time is dehydrated by a dehydrator 38 which is a dehydration means by storage mixing 33 and sludge generated in the pressure floatation separator 15. Separate and discharge the material.
Description
본 발명은 수집된 음식물등의 폐기물에서 발생하는 고농도폐수(BOD 80,000~85,000The present invention is a high concentration wastewater (BOD 80,000 ~ 85,000) generated from waste such as collected food
ppm SS 50,000~60,000ppm)를 응집하고 가압, 탈수하여 폐수를 탈리시키고 상기폐수가 탈리된 음식물 고형물질을 발효를 위한 발효수단으로 이동시키며, 상기 탈리된 폐수는 탈수 및 가압부상시키면서 생화학적인 정화처리공정을 거쳐 음식물 폐기물에서 탈리된 탈리액등의 고농도 폐수를 효율적으로 처리 할 수 있도록 한 유지방이 많이 함유된 음식물 쓰레기의 탈리액 및 고농도 폐수처리 장치에 관한 것이다.ppm SS 50,000 ~ 60,000ppm) agglomerated, depressurized and dehydrated to remove the wastewater, and the wastewater is removed from the food solids to fermentation means for fermentation, and the desorbed wastewater is dehydrated and pressurized to carry out biochemical purification The present invention relates to a degreasing solution and a high concentration wastewater treatment apparatus for food waste containing a large amount of milk fat that can efficiently treat high concentration wastewater, such as a desorption solution desorbed from food waste through a process.
일반적으로 음식물 쓰레기와 각종 폐기물등은 그 자체를 그대로 폐기할수 없기 때문에 상기 폐기물들을 분리한 다음, 이를 소각시키거나 재활용이 가능한 폐기물을 분리하여 건조하고 이건조된 폐기물을 산업상 필요한 자원으로 재활용할수 있도록 하고 있으며, 특히 상기 음식물 쓰레기등은 슬럿지 상태로 만들어 이를 소각로나 건조로로 보내기 위하여 수집된 음식물 쓰레기를 사일로에 저장하고 있었다.In general, food waste and various wastes cannot be disposed of as they are, so that the wastes can be separated and then 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, 상기음식물 쓰레기를 처리함에 있어서는 많은수분이 함유되어 있기 때문에 상기 음식물 쓰레기를 건조하고 소각시키는 방법만으로는 상기음식물 쓰레기에 함유된 폐수를 모두 증발시키거나 처리할수 없었으며, 이에 따라 상기음식물 쓰레기에서 발생되는 폐수는 그대로 방출하게 되는일이 발생되므로써 방출되는 상기폐수에 의한 수질의오염을 더욱 악화시키는 폐단이 있었다.In addition, since the food waste contains a lot of moisture, only the method of drying and incinerating the food waste could not evaporate or treat all of the waste water contained in the food waste, and thus, the food waste generated from the food waste. The wastewater to be discharged as it is, there was a waste stage that worsens the pollution of the water by the wastewater discharged as it is generated.
또, 상기음식물 쓰레기를 그대로 매립시킬 경우에는 상기음식물 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 고안은 상기와 같은 종래의 제반 문제점을 감안하여 안출한것으로, 본고안의 수집된 음식물등의 폐기물에서 발생하는 고농도 폐수를 응집하고 가압, 탈수하여 폐수를 탈리시키고 상기폐수가 탈리된 음식물 폐기물은 발효를 위한 발효수단으로 이동 시키며, 상기 탈리된 폐수는 탈수 및 가압부상 및 생화학 처리시키면서 정화 시키도록 하므로써 상기음식물 폐기물에서 탈리된 탈리액 등의 고농도 폐수를 효율적으로 처리할수 있도록 한 유지방이 많이 함유된 음식물쓰레기의 탈리액 및 고농도 폐수처리장치를 제공하려는 것인바, 이를 이하에서 첨부한 도면에 의거하여 상세히 설명하면 다음과 같다.The present invention has been devised in view of the above-mentioned conventional problems, and condenses and pressurizes and dehydrates high-density wastewater generated from wastes such as collected foods in this paper, and desorbs the wastewater. The dewatered wastewater is dehydrated, pressurized, and biochemically treated to be purified, thereby efficiently treating high-density wastewater, such as the desorption liquor desorbed from the food waste. It is intended to provide a desorption liquid and a high concentration wastewater treatment apparatus, which will be described in detail with reference to the accompanying drawings as follows.
음식물쓰레기에서 분리된 탈리액을 협잡물제거기(4)에서 저류조(9)로 이송시켜 폐수를 파이프 응집기(14)를 통하여 가압부상분리기(15)로 이송시키고, 상기 가압부상분리기(15)에서는 폐수를 부상작용으로 부상시켜 폐수에 함유된 슬러지를 분리시켜, 이 가압부상분리기(15)에서 분리된 슬럿지와 폐수는 각각 슬럿지 저류조(33)와 생화학 반응조(21)로 보내며, 상기 파이프 응집기(14)에는 용수가 공급되는 응집제 용해수단(11-1)과 혼화제 탱크(11-2), 중화제 탱크(11-3)들을 순차적으로 연결시키고 상기 저류조(9)로부터 처리되어 가압부상분리기(15)로 이송되는 폐수는 파이프 응집기(14)에서 응집되도록 하며, 생화학 반응조(21)에는 폐수정화수단인 침전조(36)에서 안정적인 침전을 유도하기 위해 생화학반응조(21)에서 산화약품을 첨가하여 일정온도를 유지하면서 체류시킨 다음 미생물조(25), MSR반응조(30), 전기화학 반응기(32)를 거쳐 침전조(36)로 이송된다. 침전조(36)에서 침전된 상등수는 맑은물이 되어 배출되며, 이때 발생되는 침전 슬럿지는 가압부상분리기(15)에서 발생된 슬럿지와 저장혼합(33)해서 탈수 수단인 탈수기(38)로 탈수하여 고형물질을 분리 배출한다.The desorption liquid separated from the food waste is transferred from the debris remover (4) to the storage tank (9) to transfer the wastewater to the pressure flotation separator (15) through the pipe flocculator (14). The sludge contained in the wastewater by flotation by flotation is separated, and the sludge and the wastewater separated by the pressure float separator 15 are sent to the sludge storage tank 33 and the biochemical reaction tank 21, respectively, and the pipe agglomerate 14 The flocculant dissolving means (11-1), admixture tank (11-2), neutralizer tank (11-3) is supplied to the water in sequence and is processed from the storage tank (9) is transferred to the pressure flotation separator (15) The waste water to be agglomerated in the pipe agglomerator 14, the biochemical reaction tank 21 to maintain a constant temperature by adding an oxidizing agent in the biochemical reaction tank 21 to induce a stable precipitation in the sedimentation tank 36, which is a waste water purification means while doing After the retention, the microbial tank 25, the MSR reaction tank 30, and the electrochemical reactor 32 are transferred to the precipitation tank 36. The supernatant precipitated in the sedimentation tank 36 is discharged as clear water, and the sediment sludge generated at this time is dehydrated by a dehydrator 38 which is a dehydration means by storage mixing 33 and sludge generated in the pressure floatation separator 15. Separate and discharge the material.
이하에서 상기와 같이 구성된 본 발명의 작용상태를 설명한다.Hereinafter will be described the working state of the present invention configured as described above.
저류조(9)로 이송된 폐수는 일정시간 체류를 시켜 유량조정 및 균등화를 작용시켜 이송펌프(14-1)를 이용하여 유량계(14-2)를 거쳐, 파이프 응집기(14)를 경유하면서 파이프라인에 혼화제(11-1), 중화제(11-2), 응집제(11-3)를 약품펌프(12)를 이용하여 일정량의 약품을 공급한다. 이때 서로 반응하여 가압부상분리기(15)의 가압수 발생장치(15-1)에서 공급하는 가압수와 혼합되어 후록(Floc)이 형성된다. 이때 형성된 후록은 가압부상조(15)에서 상부와 하부로 각각 분리되어 물과 슬럿지가 분리된다.The wastewater transported to the storage tank 9 is allowed to stay for a certain period of time to effect flow adjustment and equalization, and then to the pipe while passing through the pipe agglomerator 14 via the flowmeter 14-2 using the transfer pump 14-1. A certain amount of chemical is supplied to the line using the chemical pump 12 with the admixture 11-1, the neutralizing agent 11-2, and the flocculant 11-3. At this time, the reaction mixture is mixed with the pressurized water supplied from the pressurized water generator 15-1 of the pressurized float separator 15 to form a floc. At this time, the formed flock is separated into the upper and lower portions in the pressure flotation tank 15 to separate the water and the sludge.
상기가압부상분리기(15)에서 분리된 물은 생화학반응조(21)로 이송시켜 일정온도를 유지, 반응시켜주며, 포기장치(25-2)를 통해 일정량의 공기를 주입하여 최적 반응의 반응조건을 만들어 준다. 이때의 반응작용으로 영양소가 분해되고 BOD물질이 현저히 감소된다.Water separated from the pressure floatation separator (15) is transferred to the biochemical reaction tank (21) to maintain and react to a constant temperature, and injects a certain amount of air through the aeration device (25-2) to determine the reaction conditions of the optimum reaction. Make it. In this reaction, nutrients are decomposed and BOD substances are significantly reduced.
생화학반응조(21)에서 월류된 원수는 미생물조(25)에서 포기를 계속하면서 주된BOD물질의 영양소 분해작용을 지속적으로 유지케하며, 일정시간이 경과하면 반응공정이 종료되고 이송펌프(27)와 라인믹서(27-1)의 사이에 반응을 위한 약품을 투입하며, 탱크(10,11-1,11-3)의 약품을 펌프(29)로 이송시켜 라인믹서(27-1)로 혼합시켜 MSR반응조(28,30)로 투입된다. 일정시간을 체류시켜 교반기(30-1)로 교반시킨다음 다음공정으로 이송된다. 이때 콜로이드성입자를 다시한번 정화작용을 거치게 한다. 이때 침전조(36)로 이송된 처리수는 정화되어 처리수조(37)로 저장되며 일정량이 차면 펌프(43)와 유량계(43-1)를 거쳐 배출부(43-2)로 배출된다. 이때 배출된 처리수는 하수처리장으로 보내어지며 지역의 사정에 따라 후속설비는 정화과정을 더 할수도 있다.The raw water overflowed from the biochemical reactor 21 keeps nutrient decomposition of the main BOD material while continuing to give up in the microbial tank 25, and after a certain time, the reaction process is terminated and the transfer pump 27 and The chemicals for the reaction are introduced between the line mixers 27-1, and the chemicals in the tanks 10, 11-1 and 11-3 are transferred to the pump 29 and mixed with the line mixers 27-1. Into the MSR reactors (28, 30). After a predetermined time, the mixture is stirred with the stirrer 30-1 and then transferred to the next step. At this time, the colloidal particles undergo purification again. At this time, the treated water transferred to the settling tank 36 is purified and stored in the treating water tank 37, and when a predetermined amount is filled, the treated water is discharged to the discharge part 43-2 through the pump 43 and the flow meter 43-1. The discharged treated water is sent to the sewage treatment plant, and depending on the local circumstances, subsequent facilities may be further purified.
공정에서 발생된 슬럿지는 슬럿지저류조(33)에 저장되며 탈수수단인 탈수기(38)를 통해 탈수처리하여 케익으로 배출수단(39)을 통해 배출되면 발효공정을 거쳐 퇴비로 변화되며 농가로 보급된다.The sludge generated in the process is stored in the sludge reservoir tank 33, and dehydrated through the dehydrator 38, which is a dehydration means, is discharged through the discharge means 39 to the cake, and then converted into compost through a fermentation process and spread to farms.
이상과 같은 본 발명은 상기와 같이 음식물 쓰레기에 함유된 수분등의 폐수를 응집, 가압, 부상작용 및 생화학적 처리등으로 폐기물과 폐수를 분리시키고 상기분리되어 탈리되는 폐수를 정화처리하여 정수되도록 하며, 상기 수분이 탈리된 음식물 쓰레기는 발효를 시킬수 있도록 하여 이를 재활용하도록하므로써 상기 음식물쓰레기에 의한 환경오염을 방지할수 있게되고, 상기폐수를 정화시켜 배출하므로써 종래와 같이 음식물쓰레기 침출수가 그대로 지반으로 침투되어 지하수나 상하수도 및 토지가 오염되는 것을 방지할수 있게되는 점등의 특징을 지닌 것이다.As described above, the present invention separates waste and wastewater by coagulation, pressurization, flotation, and biochemical treatment of wastewater such as moisture contained in food waste as described above, and purifies the wastewater that is separated and detached and purified. The food waste from which moisture is desorbed can be fermented and recycled, thereby preventing environmental pollution caused by the food waste, and by purifying and discharging the waste water, the food waste leachate is infiltrated into the ground as it is. It is characterized by lighting that can prevent groundwater, water supply and sewage, and land from being contaminated.
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