KR102376024B1 - Wastewater treatment equipment using complex-filter - Google Patents
Wastewater treatment equipment using complex-filter Download PDFInfo
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- KR102376024B1 KR102376024B1 KR1020210079094A KR20210079094A KR102376024B1 KR 102376024 B1 KR102376024 B1 KR 102376024B1 KR 1020210079094 A KR1020210079094 A KR 1020210079094A KR 20210079094 A KR20210079094 A KR 20210079094A KR 102376024 B1 KR102376024 B1 KR 102376024B1
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- 238000004065 wastewater treatment Methods 0.000 title claims abstract description 22
- 238000006243 chemical reaction Methods 0.000 claims abstract description 43
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- 125000002777 acetyl group Chemical class [H]C([H])([H])C(*)=O 0.000 claims description 7
- -1 aldehyde compound Chemical class 0.000 claims description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 7
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
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- WPBNNNQJVZRUHP-UHFFFAOYSA-L manganese(2+);methyl n-[[2-(methoxycarbonylcarbamothioylamino)phenyl]carbamothioyl]carbamate;n-[2-(sulfidocarbothioylamino)ethyl]carbamodithioate Chemical compound [Mn+2].[S-]C(=S)NCCNC([S-])=S.COC(=O)NC(=S)NC1=CC=CC=C1NC(=S)NC(=O)OC WPBNNNQJVZRUHP-UHFFFAOYSA-L 0.000 description 1
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Classifications
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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
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
- B01D35/02—Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D39/00—Filtering material for liquid or gaseous fluids
- B01D39/14—Other self-supporting filtering material ; Other filtering material
-
- 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
- C02F1/40—Devices for separating or removing fatty or oily substances or similar floating material
-
- 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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
- C02F3/106—Carbonaceous materials
-
- 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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
- C02F3/107—Inorganic materials, e.g. sand, silicates
-
- 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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/105—Characterized by the chemical composition
- C02F3/108—Immobilising gels, polymers or the like
-
- 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
- C02F3/02—Aerobic processes
- C02F3/10—Packings; Fillings; Grids
- C02F3/109—Characterized by the shape
-
- 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
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/1205—Particular type of activated sludge processes
- C02F3/1215—Combinations of activated sludge treatment with precipitation, flocculation, coagulation and separation of phosphates
-
- 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
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
- C02F3/20—Activated sludge processes using diffusers
-
- 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
- C02F3/30—Aerobic and anaerobic processes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Organic Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Biological Treatment Of Waste Water (AREA)
Abstract
본 발명은 복합필터를 이용한 하·폐수 처리장치에 관한 것으로, 상기 복합필터를 이용한 하·폐수 처리장치는 오랜기간 연속사용이 가능하고 재사용이 가능한 형태의 복합필터를 구비하고, 하·폐수와 복합필터와의 반응시간 및 면적을 넓힐 수 있는 반응조를 구비함으로써, 유지비를 절감하면서 정화효율을 향상시킬 수 있는 유용한 효과를 달성할 수 있다.The present invention relates to a sewage and wastewater treatment device using a composite filter. The sewage and wastewater treatment device using the composite filter has a composite filter that can be used continuously for a long period of time and is reusable, and is equipped with a composite filter that can be used continuously for a long period of time and is reusable. By providing a reaction tank that can expand the reaction time and area with the filter, it is possible to achieve the useful effect of improving purification efficiency while reducing maintenance costs.
Description
본 발명은 복합필터를 이용한 하·폐수 처리장치에 관한 것으로, 구체적으로, 하·폐수 처리과정에서 하·폐수와 복합필터의 반응시간을 증가시키기 위한 중간벽을 구비하는 반응조를 포함하는 하·폐수 처리장치에 관한 것이다.The present invention relates to a sewage and wastewater treatment device using a composite filter, and specifically, to a sewage and wastewater treatment device including a reaction tank with an intermediate wall to increase the reaction time of the sewage and wastewater and the composite filter in the sewage and wastewater treatment process. It's about processing equipment.
안전하고 위생적인 식수 공급은 인간의 삶에 필요한 요소이다. 하지만 수문학적 변동성, 기후변화에 따른 오염, 도시화 등으로 인해 수많은 사람들이 물 부족과 열악한 위생으로 인한 질병에 노출되어 있다. 산업의 발달에 따른 대기와 토양오염은 점오염원과 비점오염원을 통해 최종적으로 수질오염을 일으킨다. 또한, 축산업 및 양식업의 대규모화로 인한 분뇨배출량의 급증으로 인해 더욱 심각해졌다. 이와 같이 수질 환경의 오염이 진행되면서 부영양화, 생태계 파괴 등 다양한 환경 변화가 발생하고 있으며, 이를 해결하기 위하여 환경 규제 및 환경 회복에 관한 움직임이 전 세계적으로 가속화되고 있다.A safe and hygienic supply of drinking water is a necessity for human life. However, due to hydrological variability, pollution caused by climate change, and urbanization, many people are exposed to diseases caused by water shortage and poor sanitation. Air and soil pollution resulting from industrial development ultimately causes water pollution through point and non-point pollution sources. In addition, it has become more serious due to the rapid increase in excrement emissions due to the large-scale livestock and aquaculture industries. As the pollution of the water environment progresses, various environmental changes such as eutrophication and ecosystem destruction are occurring, and in order to solve these problems, movements regarding environmental regulations and environmental recovery are accelerating around the world.
일반적으로 종래의 국내 하·폐수의 처리방법으로 물리적 처리는 하·폐수 중의 고형물을 중력에 의해 액체로부터 분리하거나 또는 기타의 물리적 방법으로 처리하는 공법으로 처리의 한계성이 있고, 화학적 처리는 화학 약품을 하·폐수에 첨가하여 중화 또는 pH조정, 산화 환원, 응집 침전, 흡착등의 처리공법으로 화학약품 비용 및 슬러지 발생량의 증가에 따른 처리비용이 매우 높으며, 전기분해를 이용한 하수처리 역시 처리비용이 높다는 문제점을 가지고 있다. 그에 따라서 미생물을 이용한 활성슬러지법이 개발되고 있으나 활성미생물에 의한 영양염류 제거율의 신뢰도가 낮다는 문제점과 상기 종래의 수처리법들을 실시하기 위해서 대규모 설비가 필요하다는 문제점이 있다.In general, as a conventional domestic sewage and wastewater treatment method, physical treatment is a method of separating solids in sewage and wastewater from liquid by gravity or treating them by other physical methods, which has limitations in treatment, and chemical treatment involves the use of chemicals. Treatment costs are very high due to the increase in chemical costs and sludge generation due to treatment methods such as neutralization or pH adjustment by adding to sewage and wastewater, oxidation reduction, coagulation, precipitation, and adsorption. Sewage treatment using electrolysis also has high treatment costs. There is a problem. Accordingly, activated sludge methods using microorganisms are being developed, but there are problems in that the reliability of the nutrient removal rate by activated microorganisms is low and large-scale facilities are required to implement the conventional water treatment methods.
이에, 업계에서는 미생물을 이용한 하·폐수 처리에 있어서 정화효율을 향상시키면서 조립식 구조를 가져 설치 및 운영이 편리하고, 이를 통해 유지비를 저감할 수 있는 기술개발을 요구하는 실정에 있다.Accordingly, the industry is demanding the development of technology that can improve purification efficiency in sewage and wastewater treatment using microorganisms, have a prefabricated structure, make installation and operation convenient, and thereby reduce maintenance costs.
이러한 업계에서의 요구에 부응함과 더불어 종래의 미생물을 이용한 하·폐수 처리방법을 개선하기 위한 기술로서, 1차적으로 SM칩이 내장된 반응조를 이용하여 산화환원반응을 실시하여 폐수처리의 효과를 높이는 하·폐수 처리기술이 개시되어 있다.In addition to meeting these industry demands, it is a technology to improve the conventional sewage and wastewater treatment method using microorganisms. It primarily performs an oxidation-reduction reaction using a reaction tank with a built-in SM chip to improve the effect of wastewater treatment. Sewage and wastewater treatment technology has been disclosed.
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본 발명은 상술한 종래의 문제점을 해소 및 이를 감안하여 안출된 것으로서, 유지비를 절감하면서도 정화효율을 높일 수 있는 하·폐수 처리 장치를 제공하는데 그 목적이 있다.The present invention was developed in consideration of and to solve the above-described conventional problems, and its purpose is to provide a sewage and wastewater treatment device that can increase purification efficiency while reducing maintenance costs.
본 발명에서는 최초 유입되는 원수내 슬러지를 필터링하고, 내부에 충진된 복합필터에 의해 1차 미생물 분해를 실시하는 미생물 분해조; 전처리부에서 처리된 처리수를 내부에 충진된 복합필터에 충진된 미생물로 처리수를 정화하는 제1, 제2 및 제3 반응조; 및 제2 및 제3 반응조 사이에 구비되어 내부에 복합필터가 충진되고, 내부가 무산소 상태가 형성되어 질소를 처리하는 무산소조;로 이루어지고,
상기 미생물 분해조, 제1 반응조, 제2 반응조, 무산소조 및 제3 반응조는 유입관 및 노즐이 설치되어 폐수 및 전처리 과정을 거친 처리수를 유입하고, 하방으로 낙하시키는 덮개부; 상기 덮개부에서 유입되는 처리수를 내부에 복합필터가 충진되어 정화하는 중간처리단과 상기 중간처리단 내부로 산소를 공급하는 공기유입로와 하방으로 처리수를 보내기 위해 다수개의 중공이 형성되고 하부면을 이루는 다공판을 구비하는 중간처리부; 상기 중간처리부에서 처리된 처리수를 내부에 복합필터가 충진되어 정화하는 하부처리단과, 정화 처리된 처리수를 저장하는 집수정 및 상기 하부처리단에서 집수정으로 처리수가 통과되는 다공질 금속으로 이루어진 다공금속판을 포함하는 하부처리부;로 이루어지며,
상기 미생물 분해조 이전에 최초 유입되는 폐수를 스크린에 의하여 부유 물질 및 무기물을 제거하는 부유물 제거조; 부유 물질 및 무기물이 제거된 처리수에 응집제를 투여하여 응집제에 의하여 미세 부유물질 및 무기물을 제거하는 전처리조를 포함하는 하폐수 처리장치에 있어서,
상기 중간처리부는 중간처리단 내부를 좌우로 구획하도록 구비된 중간벽을 구비하되, 상기 중간벽의 상단 또는 하단은 오픈(open)된 형태로 이루어지고,
상기 중간처리부의 중간벽은 2개 이상 구비하되, 각각의 중간벽은 평행을 이루고, 평행을 이룬 두개의 중간벽은 서로 다른 위치가 오픈된 형태이며,
상기 중간벽은 2개의 중간벽을 통해 제1, 제2 및 제3 공간부를 포함하되, 상기 제1 공간부는 질소 처리 미생물을 포함하고, 제2 공간부는 황 처리 미생물을 포함하고, 제3 공간부 질소 처리 미생물 또는 황 처리 미생물을 포함하며,
상기 황 처리 미생물은 KD-1212 균주 및 DAH-1056 균주 중 어느 하나 이상을 포함하고, 상기 질소 처리 미생물은 바실러스 아리아바타이(Bacillus aryabhattai) 균주 및 비브리오 네오칼레도니쿠스(Vibrio neocaledonicus) 균주 중 어느 하나 이상을 포함하며,
상기 중간벽은 일면 또는 양면에 활성탄 또는 산화아연을 분산시켜 구비함으로써 중간처리부에서 발생하는 유독가스를 제거하고, 상기 활성탄을 사용하는 경우에는 암모니아 또는 질산과 혼합하여 100~200℃의 온도로 열처리하여 활성탄 표면에 질소 작용기를 포함시키며,
상기 복합필터는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌 중 어느 하나 이상으로 형성된 다공성의 발포 고분자로 구성되고, 상기 고분자에 활성탄 및 제올라이트의 흡착물질이 분산된 형태로서,
상기 다공성의 발포 고분자는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌으로 구성된 군에서 선택된 발포성 고분자 5~9중량%, 알데하이드계 화합물 5∼9중량%, 물 72∼88중량%, 활성탄 및 제올라이트 분말의 흡착물질 2∼10중량%를 포함하고, 공극률이 85% 이상인 것인 복합필터를 이용한 하폐수 처리장치를 제공한다.The present invention includes a microbial decomposition tank that filters sludge in raw water that is initially introduced and performs primary microbial decomposition by a composite filter filled therein; First, second and third reaction tanks for purifying the treated water treated in the pre-treatment unit with microorganisms filled in a composite filter filled therein; and an anoxic tank provided between the second and third reaction tanks, the inside of which is filled with a composite filter, and an anoxic state is formed inside to process nitrogen.
The microbial decomposition tank, the first reaction tank, the second reaction tank, the anoxic tank, and the third reaction tank include a cover portion installed with an inlet pipe and a nozzle to introduce wastewater and treated water that has undergone a pretreatment process and allow it to fall downward; An intermediate treatment stage that purifies the treated water flowing in from the cover with a composite filter inside, an air inlet that supplies oxygen to the inside of the intermediate treatment stage, and a plurality of hollows are formed to send the treated water downward, and the lower surface An intermediate processing unit provided with a perforated plate forming a; A lower treatment stage that purifies the water treated in the intermediate treatment unit by filling it with a composite filter, a sump that stores the purified treated water, and a pore made of porous metal through which the treated water passes from the lower treatment stage to the sump. It consists of a lower processing part including a metal plate,
a suspended matter removal tank that removes suspended substances and inorganic substances by screening the wastewater initially introduced before the microbial decomposition tank; In the wastewater treatment device, which includes a pretreatment tank for removing fine suspended substances and inorganic substances by administering a coagulant to the treated water from which suspended substances and inorganic substances have been removed,
The intermediate processing unit is provided with an intermediate wall that divides the interior of the intermediate processing unit to the left and right, and the upper or lower end of the intermediate wall is open,
The intermediate processing unit has two or more intermediate walls, each intermediate wall is parallel, and the two parallel intermediate walls are open at different positions,
The intermediate wall includes first, second and third spaces through the two intermediate walls, wherein the first space includes nitrogen-treated microorganisms, the second space includes sulfur-treated microorganisms, and the third space includes Includes nitrogen-processing microorganisms or sulfur-processing microorganisms,
The sulfur-treated microorganism includes any one or more of the KD-1212 strain and the DAH-1056 strain, and the nitrogen-treated microorganism includes any one or more of the Bacillus aryabhattai strain and the Vibrio neocaledonicus strain. Includes,
The intermediate wall is equipped with activated carbon or zinc oxide dispersed on one or both sides to remove toxic gases generated in the intermediate treatment section. When the activated carbon is used, it is mixed with ammonia or nitric acid and heat treated at a temperature of 100 to 200 ° C. It contains a nitrogen functional group on the surface of activated carbon,
The composite filter is composed of a porous foamed polymer made of one or more of polyvinyl acetal, polyurethane, and polystyrene, and the adsorption material of activated carbon and zeolite is dispersed in the polymer,
The porous foam polymer includes 5 to 9% by weight of a foamable polymer selected from the group consisting of polyvinyl acetal, polyurethane, and polystyrene, 5 to 9% by weight of an aldehyde compound, 72 to 88% by weight of water, activated carbon, and an adsorbent of zeolite powder. A wastewater treatment device using a composite filter containing 2 to 10% by weight and having a porosity of 85% or more is provided.
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본 발명에 따르면, 오랜기간 연속사용이 가능하고 재사용이 가능한 형태의 복합필터를 구비하고, 하·폐수와 복합필터와의 반응시간 및 면적을 넓힐 수 있는 반응조를 구비함으로써, 유지비를 절감하면서 정화효율을 향상시킬 수 있는 유용한 효과를 달성할 수 있다.According to the present invention, by providing a composite filter that can be used continuously for a long period of time and is reusable, and by providing a reaction tank that can expand the reaction time and area between sewage and wastewater and the composite filter, maintenance costs are reduced while purification efficiency is provided. Useful effects that can improve can be achieved.
또한, 본 발명에 따르면, 중간처리부의 복합필터의 기공을 제어함으로써 중간처리부로 유입되는 원수 또는 처리수의 유속을 제어하고 슬러지에 의한 막힘현상을 최소화할 수 있다.In addition, according to the present invention, by controlling the pores of the composite filter of the intermediate treatment unit, it is possible to control the flow rate of raw water or treated water flowing into the intermediate treatment unit and minimize clogging due to sludge.
도 1은 본 발명의 일 실시예에 따른 하·폐수 처리장치의 사시도이다.
도 2는 본 발명의 일 실시예에 따른 덮개부의 참고도이다.
도 3은 본 발명의 일 실시예에 따른 중간처리부의 참고도이다.
도 4는 본 발명의 일 실시예에 따른 하부처리부의 참고도이다.Figure 1 is a perspective view of a sewage and wastewater treatment device according to an embodiment of the present invention.
Figure 2 is a reference diagram of a cover portion according to an embodiment of the present invention.
Figure 3 is a reference diagram of an intermediate processing unit according to an embodiment of the present invention.
Figure 4 is a reference diagram of a lower processing unit according to an embodiment of the present invention.
본 발명에 대해 첨부한 도면을 참조하여 바람직한 실시예를 설명하면 다음과 같으며, 이와 같은 상세한 설명을 통해서 본 발명의 목적과 구성 및 그에 따른 특징들을 보다 잘 이해할 수 있게 될 것이다.Preferred embodiments of the present invention will be described with reference to the accompanying drawings as follows. Through this detailed description, the purpose and configuration of the present invention and its characteristics will be better understood.
본 발명은 하·폐수 처리장치에 있어서,The present invention relates to a sewage and wastewater treatment device,
상기 처리장치는,The processing device is,
최초 유입되는 원수내 슬러지를 필터링하고, 내부에 충진된 복합필터에 의해 1차 미생물 분해를 실시하는 미생물 분해조;A microbial decomposition tank that filters the sludge in the raw water that is initially introduced and performs primary microbial decomposition by a composite filter filled inside;
전처리부에서 처리된 처리수를 내부에 충진된 복합필터에 충진된 미생물로 처리수를 정화하는 제1, 제2 및 제3 반응조; 및First, second and third reaction tanks for purifying the treated water treated in the pre-treatment unit with microorganisms filled in a composite filter filled therein; and
제2 및 제3 반응조 사이에 구비되어 내부에 복합필터가 충진되고, 내부가 무산소 상태가 형성되어 질소를 처리하는 무산소조;로 이루어지고,It consists of an anoxic tank provided between the second and third reaction tanks, the inside of which is filled with a composite filter, and an anoxic state is formed inside to process nitrogen,
상기 미생물 분해조, 제1 반응조, 제2 반응조, 무산소조 및 제3 반응조는 유입관 및 노즐이 설치되어 폐수 및 전처리 과정을 거친 처리수를 유입하고, 하방으로 낙하시키는 덮개부;The microbial decomposition tank, the first reaction tank, the second reaction tank, the anoxic tank, and the third reaction tank include a cover portion installed with an inlet pipe and a nozzle to introduce wastewater and treated water that has undergone a pretreatment process and allow it to fall downward;
상기 덮개부에서 유입되는 처리수를 내부에 복합필터가 충진되어 정화하는 중간처리단과 상기 중간처리단 내부로 산소를 공급하는 공기유입로와 하방으로 처리수를 보내기 위해 다수개의 중공이 형성되고, 하부면을 이루는 다공판과 중간처리단 내부를 좌우로 구획하도록 구비된 중간벽을 구비하되, 상기 중간벽의 상단 또는 하단은 오픈(open)된 형태로 이루어지는 중간처리부; 및An intermediate treatment stage that purifies the treated water flowing in from the cover with a composite filter inside, an air inlet that supplies oxygen to the inside of the intermediate treatment stage, and a plurality of hollow holes are formed to send the treated water downward, and a lower part. An intermediate treatment unit comprising a perforated plate forming a surface and an intermediate wall configured to divide the interior of the intermediate treatment unit to the left and right, wherein the upper or lower end of the intermediate wall is open. and
상기 중간처리부에서 처리된 처리수를 내부에 복합필터가 충진되어 정화하는 하부처리단과, 정화 처리된 처리수를 저장하는 집수정 및 상기 하부처리단에서 집수정으로 처리수가 통과되는 다공질 금속으로 이루어진 다공금속판을 포함하는 하부처리부;로 이루어지며,A lower treatment stage that purifies the water treated in the intermediate treatment unit by filling it with a composite filter, a sump that stores the purified treated water, and a pore made of porous metal through which the treated water passes from the lower treatment stage to the sump. It consists of a lower processing part including a metal plate,
상기 복합필터는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌 중 어느 하나 이상으로 형성된 다공성의 발포 고분자로 구성되고, 상기 고분자에 활성탄 및 제올라이트 분말이 분산된 형태이고, 산화환원반응에 의하여 외부는 호기성 미생물이 활성화되고, 내부는 혐기성 미생물이 활성화되는 것을 특징으로 하는 하·폐수 처리장치를 제공한다. The composite filter is composed of a porous foam polymer made of one or more of polyvinyl acetal, polyurethane, and polystyrene, and activated carbon and zeolite powder are dispersed in the polymer, and aerobic microorganisms are activated on the outside through a redox reaction. It provides a sewage and wastewater treatment device characterized in that anaerobic microorganisms are activated inside.
도 1은 본 발명의 일 실시예에 따른 하·폐수 처리장치의 사시도로 도 1을 참고하여 하기에 구체적으로 서술한다.Figure 1 is a perspective view of a sewage and wastewater treatment device according to an embodiment of the present invention, which will be described in detail below with reference to Figure 1.
본 발명의 하폐수 처리장치는 최초 유입되는 원수내 슬러지를 필터링하고, 내부에 충진된 복합필터에 의해 1차 미생물 분해를 실시하는 미생물 분해조(10); 상기 미생물 분해조(10)에서 처리된 처리수를 내부에 충진된 산화환원반응으로 활성화되는 복합필터에 부착된 미생물로 처리수를 정화하는 제1 반응조(20), 제2 반응조(30), 제3 반응조(50); 및 상기 제2 반응조(30) 및 제3 반응조(50) 사이에 위치하여 내부에 복합필터가 충진되고, 내부를 무산소 상태가 되도록 하여 질소를 처리하는 무산소조(40);로 구성된다.The wastewater treatment device of the present invention includes a microbial decomposition tank (10) that filters sludge in raw water that is initially introduced and performs primary microbial decomposition by a composite filter filled therein ; A first reaction tank (20), a second reaction tank (30), and a second reaction tank (20), which purify the treated water treated in the microbial decomposition tank (10) with microorganisms attached to a complex filter filled inside and activated by a redox reaction. 3 reaction tank (50); And an anoxic tank (40) located between the second reaction tank (30) and the third reaction tank (50) , filled with a composite filter inside , and treating nitrogen by making the inside an anoxic state.
본 발명은 미생물 분해조(10), 제1 반응조(20), 제2 반응조(30), 무산소조(40) 및 제3 반응조(50)의 순으로 이루어지고, 상기의 분해조(10), 제1 반응조(20), 제2 반응조(30), 무산소조(40) 및 제3 반응조(50)의 내부에는 복합필터가 충진되어 있으며, 도시되어 있지 않으나, 미생물 분해조 이전에 전처리 설비로 스크린 장치가 구비되어 스크린에 의하여 부유 물질 및 무기물을 제거하는 부유물 제거조; 및 응집제에 의하여 미세 부유물질 및 무기물을 제거하는 전처리조를 더 포함할 수 있다.The present invention consists of a microbial digestion tank (10), a first reaction tank (20), a second reaction tank (30), an anoxic tank (40), and a third reaction tank (50) in that order, and the digestion tank (10) The interior of the first reaction tank (20), the second reaction tank (30), the anoxic tank (40), and the third reaction tank (50) is filled with a composite filter. Although not shown, a screen device is used as a pretreatment facility before the microbial decomposition tank. A suspended matter removal tank is provided to remove suspended substances and minerals using a screen; And it may further include a pretreatment tank for removing fine suspended solids and inorganic substances using a coagulant.
도 2는 본 발명의 일 실시예에 따른 덮개부(60)의 참고도이고, 도 3은 본 발명의 일 실시예에 따른 중간처리부(70)의 참고도이며, 도 4는 본 발명의 일 실시예에 따른 하부처리부(80)의 참고도로 도 2 내지 4를 참고하여 하기에 상기 장치를 구체적으로 서술한다.Figure 2 is a reference diagram of the cover part 60 according to an embodiment of the present invention, Figure 3 is a reference diagram of the intermediate processing unit 70 according to an embodiment of the present invention, and Figure 4 is an embodiment of the present invention. The device will be described in detail below with reference to FIGS. 2 to 4 as a reference diagram of the lower processing unit 80 according to an example.
상기 미생물 분해조(10), 제1 반응조(20), 제2 반응조(30) , 무산소조(40) 및 제3 반응조(50)는 덮개(62), 유입관(64) 및 노즐이 설치되어 원수 및 전처리 과정을 마친 처리수를 유입하고, 하방으로 낙하시키는 덮개부(60); 상기 덮개부(60)에서 유입되는 처리수를 내부에 복합필터가 충진되어 정화하는 중간처리단(72)과 상기 중간처리단(72) 내부로 산소를 공급하는 공기유입로(미도시)와 하방으로 처리수를 보내기 위해 다수개의 중공이 형성되고 하부면을 이루는 다공판(76) 및 중간처리단 내부를 좌우로 구획하도록 구비된 중간벽을 구비하되, 상기 중간벽의 상단 또는 하단은 오픈(open)된 형태로 이루어지는 중간처리부(70); 및 상기 중간처리부(70)에서 처리된 처리수를 내부에 복합필터가 충진되어 정화하는 하부처리단(82)과, 정화 처리된 처리수를 저장하는 집수정(84) 및 상기 하부처리단(82)에서 집수정(84)으로 처리수가 통과되는 다공질 금속으로 이루어진 다공금속판(86)을 포함하는 하부처리부(80);로 이루어진다.The microbial decomposition tank 10, the first reaction tank 20, the second reaction tank 30, the anoxic tank 40, and the third reaction tank 50 are equipped with a cover 62, an inlet pipe 64, and a nozzle to provide raw water. and a cover part 60 that introduces treated water that has completed the pre-treatment process and causes it to fall downward; An intermediate treatment stage (72) that purifies the treated water flowing in from the cover part (60) with a complex filter inside, an air inlet (not shown) that supplies oxygen into the intermediate treatment stage (72), and a lower part. It is provided with a porous plate 76 forming the lower surface and forming a plurality of hollow holes to send the treated water to the bottom, and an intermediate wall provided to divide the interior of the intermediate treatment stage to the left and right, and the top or bottom of the intermediate wall is open (open). ) an intermediate processing unit 70 in the form of; and a lower treatment stage 82 that purifies the treated water treated in the intermediate treatment unit 70 by filling a complex filter therein , a collection well 84 that stores the purified treated water, and the lower treatment stage 82. It consists of a lower treatment unit 80 including a porous metal plate 86 made of porous metal through which treated water passes from ) to the water collection well 84.
상기 덮개부의 유입관은 중간처리부의 중간벽이 구비된 경우 중간처리부의 좌측에 형성된 유입관을 사용하여 중간처리부 내의 처리수가 중간벽을 따라 원활하게 이동하도록 한다. 또한, 상기 덮개부의 노즐은 헬리코일 노즐(스파이럴 노즐)(66)을 사용하여 하부로 원수 및 처리수를 넓게 분사한다.When the inlet pipe of the cover part is provided with a middle wall of the intermediate treatment section, the inlet pipe formed on the left side of the intermediate treatment section is used to allow the treated water in the intermediate treatment section to move smoothly along the middle wall. In addition, the nozzle of the cover part uses a helicoil nozzle (spiral nozzle) 66 to widely spray raw water and treated water downward.
구체적으로, 상기 중간처리부의 중간벽은 2개 이상 구비하되, 각각의 중간벽은 평행을 이루고, 평행을 이룬 두개의 중간벽은 서로 다른 위치가 오픈된 형태일 수 있다. 예를 들어, 중간벽이 2개 구비된 경우, 하나의 중간벽은 덮개부로부터 아래쪽으로 형성되며 하단부가 오픈된 형태로 처리수가 다음 공간으로 이동하도록 하고, 다른 하나의 중간벽은 중간처리부의 바닥면으로부터 위쪽으로 형성되며 상단부가 오픈된 형태로 처리수가 다음 공간으로 이동하도록 한다. 이와 같이 중간처리부 내에 중간벽을 형성함에 따라 유입된 처리수와 복합필터의 반응시간 및 반응하는 면적이 증가하여 정화효율을 향상시킬 수 있다. Specifically, the intermediate processing unit may have two or more intermediate walls, and each intermediate wall may be parallel, and the two parallel intermediate walls may be open at different positions. For example, when two intermediate walls are provided, one intermediate wall is formed downward from the cover and has an open lower end to allow treated water to move to the next space, and the other intermediate wall is formed at the bottom of the intermediate treatment section. It is formed upward from the surface and is open at the top to allow treated water to move to the next space. In this way , by forming an intermediate wall within the intermediate treatment unit, the reaction time and reaction area between the inflow treated water and the composite filter increase, thereby improving purification efficiency.
상기 중간벽은 일면 또는 양면에 활성탄 또는 산화아연을 분산시켜 구비된 형태일 수 있다. 상기 활성탄을 사용하는 경우에는 암모니아 또는 질산과 혼합하여 100~200℃의 온도로 열처리하여 활성탄 표면에 질소 작용기를 포함할 수 있다. 상기와 같은 활성탄 또는 산화아연을 중간벽에 분산시켜 구비함에 따라 중간처리부에서 발생하는 유독가스를 제거할 수 있다.The intermediate wall may be provided by dispersing activated carbon or zinc oxide on one or both sides. When using the activated carbon, it may be mixed with ammonia or nitric acid and heat treated at a temperature of 100 to 200° C. to include a nitrogen functional group on the surface of the activated carbon. By dispersing activated carbon or zinc oxide as described above in the intermediate wall, toxic gases generated in the intermediate treatment section can be removed.
또한, 상기 중간처리부는 중간벽에 의해 3개 이상의 공간부로 나뉘는데, 이때, 각 공간부에 포함되는 미생물의 종류가 서로 상이할 수 있고, 상기 미생물을 질소 처리 미생물 또는 황 처리 미생물일 수 있다. 구체적으로, 2개의 중간벽으로 이루어진 경우 제1, 제2 및 제3 공간부를 포함하고, 상기 제1 공간부는 질소 처리 미생물을 포함하고, 제2 공간부는 황 처리 미생물을 포함하고, 제3 공간부 질소 처리 미생물 또는 황 처리 미생물을 포함할 수 있고, 이와 반대의 경우도 포함할 수 있다.In addition, the intermediate treatment unit is divided into three or more spaces by an intermediate wall. At this time, the types of microorganisms included in each space may be different, and the microorganisms may be nitrogen-treated microorganisms or sulfur-treated microorganisms. Specifically, when it is composed of two intermediate walls, it includes first, second, and third space parts, wherein the first space part contains nitrogen-treated microorganisms, the second space part contains sulfur-treated microorganisms, and the third space part contains the sulfur-treated microorganisms. It may include nitrogen-treated microorganisms or sulfur-treated microorganisms , and vice versa.
상기 황 처리 미생물은 KD-1212 균주 및 DAH-1056 균주 중 어느 하나 이상을 포함하고, 상기 질소 처리 미생물은 바실러스 아리아바타이(Bacillus aryabhattai) 균주 및 비브리오 네오칼레도니쿠스(Vibrio neocaledonicus) 균주 중 어느 하나 이상을 포함한다.The sulfur-treated microorganism includes any one or more of the KD-1212 strain and the DAH-1056 strain, and the nitrogen-treated microorganism includes any one or more of the Bacillus aryabhattai strain and the Vibrio neocaledonicus strain. Includes.
일반적으로 하·폐수 내에 포함되어 있는 질소 및 황을 제거하기 위해서는 서로 다른 반응조에 미생물을 각각 넣어야 하지만, 중간벽을 포함함으로써 하나의 반응조에서 질소 및 황을 동시에 처리할 수 있는 이점이 있다.Generally, in order to remove nitrogen and sulfur contained in sewage and wastewater, microorganisms must be placed in different reaction tanks, but by including an intermediate wall, there is an advantage that nitrogen and sulfur can be treated simultaneously in one reaction tank .
상기 복합필터는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌 중 어느 하나 이상으로 형성된 다공성의 발포 고분자로 구성되고, 상기 고분자에 활성탄 및 제올라이트가 분산된 형태이고, 상기 다공성의 발포 고분자는 산화환원반응에 의하여 외부는 호기성 미생물이 활성화되고, 내부는 혐기성 미생물이 활성화되며, 출구부에는 호기성과 혐기성균이 번식되어 슬러지를 처리한다. The composite filter is composed of a porous foamed polymer made of one or more of polyvinyl acetal, polyurethane, and polystyrene, and activated carbon and zeolite are dispersed in the polymer , and the porous foamed polymer is exposed to the outside through a redox reaction. Aerobic microorganisms are activated, anaerobic microorganisms are activated inside, and aerobic and anaerobic bacteria grow at the outlet to treat sludge.
구체적으로, 상기 다공성의 발포 고분자는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌으로 구성된 군에서 선택된 발포성 고분자 5~9중량%, 알데하이드계 화합물 5∼9중량%, 물 72∼88중량%, 활성탄 및 제올라이트 분말의 흡착물질 2∼10중량%, 가용성 물질 등을 혼합하여 가열 용융시켜 제조한 것이고, 공극률이 85% 이상 또는 90% 이상이다. Specifically, the porous foam polymer includes 5 to 9% by weight of a foamable polymer selected from the group consisting of polyvinyl acetal, polyurethane, and polystyrene, 5 to 9% by weight of an aldehyde compound, 72 to 88% by weight of water, activated carbon, and zeolite powder. It is manufactured by mixing and heating and melting 2 to 10% by weight of adsorbed substances and soluble substances, and has a porosity of 85% or more or 90% or more.
상기와 같은 다공성의 발포 고분자를 사용함으로써 복합필터의 전체 압력손실을 줄이고 미생물의 부착 및 고분자 내부로의 물질전달률이 높아 복합필터의 성능을 높게 유기할 수 있다. 또한, 10년 이상 오랜 기간동안 연속사용이 가능하고, 세척하여 재사용이 가능하여 처리장치의 유지비를 절감할 수 있는 이점이 있다.By using the porous foamed polymer as described above, the overall pressure loss of the composite filter can be reduced and the performance of the composite filter can be improved by increasing the attachment of microorganisms and the mass transfer rate into the polymer. In addition, it can be used continuously for a long period of time, more than 10 years, and can be washed and reused, which has the advantage of reducing the maintenance cost of the treatment device.
삭제delete
상기 활성탄은 황과 활성탄을 4~6:6~4의 비율로 혼합하여 100~200℃의 온도로 열처리하여 제조된 황이 결합된 활성탄일 수 있다.The activated carbon may be sulfur-bound activated carbon prepared by mixing sulfur and activated carbon in a ratio of 4-6:6-4 and heat-treating the mixture at a temperature of 100-200°C.
상기 활성탄을 포함하여 질소, 인 및 색도제거에 탁월한 효과가 있다.Including the activated carbon, it is excellent at removing nitrogen, phosphorus, and coloring.
또한, 상기 복합필터는 50㎛ 내지 10mm, 100㎛ 내지 10mm 또는 100㎛ 내지 5mm의 기공을 가질 수 있다.Additionally, the composite filter may have pores of 50㎛ to 10mm, 100㎛ to 10mm, or 100㎛ to 5mm.
상기 중간처리부의 상부와 하부에 복합필터를 구비할 수 있고, 복합필터의 기공을 제어함으로써 중간처리부로 유입되는 원수 또는 처리수의 유속을 제어하고 슬러지에 의한 막힘현상을 최소화할 수 있다. A composite filter can be provided at the upper and lower portions of the intermediate treatment section, and by controlling the pores of the composite filter, the flow rate of raw water or treated water flowing into the intermediate treatment section can be controlled and clogging due to sludge can be minimized.
상기 공기유입로(미도시)는 중간처리부(70) 및 하부처리부(80) 상부에 위치하고, 외부에서 시작되는 공기유입로가 내부유입로 보다 높게 형성되어 처리수가 외부로 배출되는 것을 방지한다. 또한, 상기 공기유입로는 무산소조에 구성시키지 않는 것이 바람직하다.The air inflow path (not shown) is located above the intermediate treatment unit 70 and the lower treatment unit 80, and the air inflow path starting from the outside is formed higher than the internal inflow path to prevent treated water from being discharged to the outside. Additionally, it is preferable not to configure the air inflow path in an anoxic tank.
중간처리단(72)과 하부처리단(82)에서 상기 조립수단(78)이 설치되어 있지 않는 가장자리는 각 중간처리단(72) 및 하부처리단(82) 내부를 통해 집수정에 저장된 처리수를 상부로 보내는 배출관(90)이 연결 설치된다.The edge of the intermediate treatment stage 72 and the lower treatment stage 82 where the assembly means 78 is not installed is treated water stored in the sump through the inside of each intermediate treatment stage 72 and the lower treatment stage 82. A discharge pipe 90 that sends to the top is connected and installed.
상기 집수정(84)은 내부 일측에 다공성으로 이루어진 칸막이가 설치되어 배출파트(88)를 두고, 배출파트(88)에 위치한 배출관(90)으로 처리수를 배출한다.The water collection well (84) has a porous partition installed on one side of the interior, has a discharge part (88), and discharges treated water through a discharge pipe (90) located in the discharge part (88).
상기 배출파트(88)는 집수정(84)보다 낮은 위치로 이루어지고, 상기 칸막이는 다공성의 칸막이 또는 친수성인 재생 셀룰로오스, 초산셀룰로오스(CA) 및 폴리비닐알콜(PVA) 중 선택된 하나의 친수성 고분자막으로 이루어질 수 있다.The discharge part 88 is located at a lower position than the water collection well 84, and the partition is a porous partition or a hydrophilic polymer membrane selected from hydrophilic regenerated cellulose, cellulose acetate (CA), and polyvinyl alcohol (PVA). It can be done.
상기 다공금속판(86)은 다공질의 금속으로 니켈, 크롬, 철, 탄소, 및 망간이 혼합된 인코넬(Inconel) 금속으로 이루어질 수 있거나 일반적인 금속막을 사용할 수 있다. The porous metal plate 86 may be made of Inconel metal, which is a porous metal mixed with nickel, chromium, iron, carbon, and manganese, or a general metal film may be used.
상기 미생물 분해조(10), 제1 반응조(20), 제2 반응조(30), 무산소조(40) 및 제3 반응조(50)를 이루는 틀의 재질은 패각분말과 폴리에틸렌 또는 폴리프로필렌을 혼합하여 제조된 합성수지로 이루어진다.The material of the frame forming the microbial decomposition tank (10), the first reaction tank (20), the second reaction tank (30), the anoxic tank (40), and the third reaction tank (50) is manufactured by mixing shell powder and polyethylene or polypropylene. It is made of synthetic resin.
상기 각 조를 이루는 재질인 합성수지는 굴 또는 꼬막 등의 패각을 증류수로 3회이상 세척하고, 건조시킨 뒤 분말화 하여 60~70℃로 가열후 계면활성제로 표면처리하여 표면 극성을 낮추고 폴리에틸렌 또는 폴리프로필렌과 1:1 비율로 혼합하여 금형사출하여 제작된다. 또한, 추가로 돌로마이트, 활성 규사를 첨가하여 제조될 수 있다.The synthetic resin, which is the material that makes up each of the above groups, is made by washing the shells of oysters or cockles with distilled water at least three times, drying them, powdering them, heating them to 60-70°C, treating the surface with a surfactant to lower the surface polarity, and making it polyethylene or polypropylene. It is produced by mixing and injection molding in a 1:1 ratio. In addition, it can be manufactured by additionally adding dolomite and activated silica sand.
본 발명에 따른 하·폐수 처리장치는 호기성과 혐기성 균을 포함하고 있는 복합필터를 각 조 내부에 충진하여 하·폐수를 정화시키는 것으로 정화효율을 높였으며, 슬러지 발생을 최소화시킴으로써 슬러지 처리를 위한 추가설비를 시설이 필요하지 않고, 그에 따라서 좁은 공간에 시설할 수 있고, 유지비용을 저감할 수 있다.The sewage and wastewater treatment device according to the present invention purifies sewage and wastewater by filling the inside of each tank with a composite filter containing aerobic and anaerobic bacteria, thereby increasing purification efficiency and minimizing sludge generation, providing additional sludge treatment. There is no need for equipment, so it can be installed in a small space and maintenance costs can be reduced.
이상의 설명은, 본 발명의 구체적인 실시예에 관한 것이나 본 발명에 따른 상기 실시예는 설명의 목적으로 개시된 사항이고 본 발명의 범위를 제한하는 것으로 이해되지는 않으며, 해당 기술분야에서 통상의 지식을 가진 자라면 본 발명의 본질을 벗어나지 아니하고 개시된 실시예에 대해 다양한 변경 및 수정이 가능한 것으로 이해되어야 한다. 따라서, 이러한 모든 수정과 변경은 특허청구범위에 개시된 발명의 범위 또는 이들의 균등물에 해당하는 것으로 이해될 수 있다.The above description relates to specific embodiments of the present invention, but the embodiments according to the present invention are disclosed for illustrative purposes and are not to be understood as limiting the scope of the present invention, and those skilled in the art It should be understood that various changes and modifications can be made to the disclosed embodiments without departing from the essence of the present invention. Accordingly, all such modifications and changes may be understood as falling within the scope of the invention disclosed in the patent claims or equivalents thereof.
10: 미생물 분해조, 20: 제1 반응조, 30:제2 반응조
40: 무산소조, 50: 제3 반응조,
60: 덮개부, 62: 덮개, 64: 유입관, 66:헬리코일 노즐
70: 중간처리부, 72: 중간처리단,
74: 중간벽, 76: 다공판
80: 하부처리부, 82: 하부처리단
84: 집수정, 86: 다공금속판, 88: 배출파트
90: 배출관10: microbial digestion tank, 20: first reaction tank, 30: second reaction tank
40: anoxic tank, 50: third reaction tank,
60: cover part, 62: cover, 64: inlet pipe, 66: helicoil nozzle
70: intermediate processing unit, 72: intermediate processing stage,
74: intermediate wall, 76: perforated plate
80: lower processing unit, 82: lower processing stage
84: sump, 86: porous metal plate, 88: discharge part
90: discharge pipe
Claims (5)
상기 미생물 분해조, 제1 반응조, 제2 반응조, 무산소조 및 제3 반응조는 유입관 및 노즐이 설치되어 폐수 및 전처리 과정을 거친 처리수를 유입하고, 하방으로 낙하시키는 덮개부; 상기 덮개부에서 유입되는 처리수를 내부에 복합필터가 충진되어 정화하는 중간처리단과 상기 중간처리단 내부로 산소를 공급하는 공기유입로와 하방으로 처리수를 보내기 위해 다수개의 중공이 형성되고 하부면을 이루는 다공판을 구비하는 중간처리부; 상기 중간처리부에서 처리된 처리수를 내부에 복합필터가 충진되어 정화하는 하부처리단과, 정화 처리된 처리수를 저장하는 집수정 및 상기 하부처리단에서 집수정으로 처리수가 통과되는 다공질 금속으로 이루어진 다공금속판을 포함하는 하부처리부;로 이루어지며,
상기 미생물 분해조 이전에 최초 유입되는 폐수를 스크린에 의하여 부유 물질 및 무기물을 제거하는 부유물 제거조; 부유 물질 및 무기물이 제거된 처리수에 응집제를 투여하여 응집제에 의하여 미세 부유물질 및 무기물을 제거하는 전처리조를 포함하는 하폐수 처리장치에 있어서,
상기 중간처리부는 중간처리단 내부를 좌우로 구획하도록 구비된 중간벽을 구비하되, 상기 중간벽의 상단 또는 하단은 오픈(open)된 형태로 이루어지고,
상기 중간처리부의 중간벽은 2개 이상 구비하되, 각각의 중간벽은 평행을 이루고, 평행을 이룬 두개의 중간벽은 서로 다른 위치가 오픈된 형태이며,
상기 중간벽은 2개의 중간벽을 통해 제1, 제2 및 제3 공간부를 포함하되, 상기 제1 공간부는 질소 처리 미생물을 포함하고, 제2 공간부는 황 처리 미생물을 포함하고, 제3 공간부 질소 처리 미생물 또는 황 처리 미생물을 포함하며,
상기 황 처리 미생물은 KD-1212 균주 및 DAH-1056 균주 중 어느 하나 이상을 포함하고, 상기 질소 처리 미생물은 바실러스 아리아바타이(Bacillus aryabhattai) 균주 및 비브리오 네오칼레도니쿠스(Vibrio neocaledonicus) 균주 중 어느 하나 이상을 포함하며,
상기 중간벽은 일면 또는 양면에 활성탄 또는 산화아연을 분산시켜 구비함으로써 중간처리부에서 발생하는 유독가스를 제거하고, 상기 활성탄을 사용하는 경우에는 암모니아 또는 질산과 혼합하여 100~200℃의 온도로 열처리하여 활성탄 표면에 질소 작용기를 포함시키며,
상기 복합필터는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌 중 어느 하나 이상으로 형성된 다공성의 발포 고분자로 구성되고, 상기 고분자에 활성탄 및 제올라이트가 분산된 형태로서,
상기 다공성의 발포 고분자는 폴리비닐아세탈, 폴리우레탄, 폴리스틸렌으로 구성된 군에서 선택된 발포성 고분자 5~9중량%, 알데하이드계 화합물 5∼9중량%, 물 72∼88중량%, 활성탄 및 제올라이트 분말 2∼10중량%를 포함하고, 공극률이 85% 이상인 것인 복합필터를 이용한 하폐수 처리장치.A microbial decomposition tank that filters the sludge in the raw water that is initially introduced and performs primary microbial decomposition by a composite filter filled inside; First, second and third reaction tanks for purifying the treated water treated in the pre-treatment unit with microorganisms filled in a composite filter filled therein; and an anoxic tank provided between the second and third reaction tanks, the inside of which is filled with a composite filter, and an anoxic state is formed inside to process nitrogen.
The microbial decomposition tank, the first reaction tank, the second reaction tank, the anoxic tank, and the third reaction tank include a cover portion installed with an inlet pipe and a nozzle to introduce wastewater and treated water that has undergone a pretreatment process and allow it to fall downward; An intermediate treatment stage that purifies the treated water flowing in from the cover with a composite filter inside, an air inlet that supplies oxygen to the inside of the intermediate treatment stage, and a plurality of hollows are formed to send the treated water downward, and the lower surface An intermediate processing unit provided with a perforated plate forming a; A lower treatment stage that purifies the water treated in the intermediate treatment unit by filling it with a composite filter, a sump that stores the purified treated water, and a pore made of porous metal through which the treated water passes from the lower treatment stage to the sump. It consists of a lower processing part including a metal plate,
a suspended matter removal tank that removes suspended substances and inorganic substances by screening the wastewater initially introduced before the microbial decomposition tank; In the wastewater treatment device, which includes a pretreatment tank for removing fine suspended substances and inorganic substances by administering a coagulant to the treated water from which suspended substances and inorganic substances have been removed,
The intermediate processing unit is provided with an intermediate wall that divides the interior of the intermediate processing unit to the left and right, and the upper or lower end of the intermediate wall is open,
The intermediate processing unit has two or more intermediate walls, each intermediate wall is parallel, and the two parallel intermediate walls are open at different positions,
The intermediate wall includes first, second and third spaces through the two intermediate walls, wherein the first space includes nitrogen-treated microorganisms, the second space includes sulfur-treated microorganisms, and the third space includes Includes nitrogen-processing microorganisms or sulfur-processing microorganisms,
The sulfur-treated microorganism includes any one or more of the KD-1212 strain and the DAH-1056 strain, and the nitrogen-treated microorganism includes any one or more of the Bacillus aryabhattai strain and the Vibrio neocaledonicus strain. Includes,
The intermediate wall is equipped with activated carbon or zinc oxide dispersed on one or both sides to remove toxic gases generated in the intermediate treatment section. When the activated carbon is used, it is mixed with ammonia or nitric acid and heat treated at a temperature of 100 to 200 ° C. It contains a nitrogen functional group on the surface of activated carbon,
The composite filter is composed of a porous foam polymer made of one or more of polyvinyl acetal, polyurethane, and polystyrene, and activated carbon and zeolite are dispersed in the polymer,
The porous foam polymer includes 5 to 9% by weight of a foamable polymer selected from the group consisting of polyvinyl acetal, polyurethane and polystyrene, 5 to 9% by weight of an aldehyde compound, 72 to 88% by weight of water, activated carbon and zeolite powder 2 to 10%. A wastewater treatment device using a composite filter containing % by weight and having a porosity of 85% or more.
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