KR20090111188A - Discharged Water Treatment System and Method for Treating Discharged Water Using the Same - Google Patents
Discharged Water Treatment System and Method for Treating Discharged Water Using the Same Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 47
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- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicon dioxide Inorganic materials O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 2
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- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
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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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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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
- C02F1/30—Treatment of water, waste water, or sewage by irradiation
- C02F1/32—Treatment of water, waste water, or sewage by irradiation with ultraviolet light
- C02F1/325—Irradiation devices or lamp constructions
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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
- C02F1/72—Treatment of water, waste water, or sewage by oxidation
- C02F1/725—Treatment of water, waste water, or sewage by oxidation by catalytic oxidation
-
- 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
- C02F3/06—Aerobic processes using submerged filters
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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
- C02F3/12—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
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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
- C02F3/30—Aerobic and anaerobic processes
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/001—Runoff or storm water
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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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/002—Construction details of the apparatus
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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
- C02F2305/00—Use of specific compounds during water treatment
- C02F2305/10—Photocatalysts
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Abstract
Description
본 발명은 일체형 방류수 처리시스템 및 이를 이용한 방류수의 처리방법에 관한 것으로서, 더욱 상세하게는 소규모 또는 마을 하수처리장에서 효율적으로 사용될 수 있도록, 침지형 섬유여과기 및 침지형 자외선 소독장치가 여과소독방류조에 일체형으로 설치된 일체형 방류수 처리시스템 및 이를 이용한 방류수의 처리방법에 관한 것에 관한 것이다.The present invention relates to an integrated effluent treatment system and a method for treating effluent using the same, and more specifically, an immersion type fiber filter and an immersion type ultraviolet disinfection device are installed integrally in a filtration disinfection tank to be effectively used in a small or village sewage treatment plant. An integrated effluent treatment system and a method for treating effluent using the same.
우리나라는 지역 및 계절에 따른 강수량 변화가 심하여 안정적인 수자원 확보가 곤란한 특성을 가지고 있다. 또한 급속하게 진행된 도시화와 산업화에 따른 물 사용량의 증가와 녹지면적의 감소, 콘크리트, 아스팔트화 등의 불투수층 면적이 증가하면서 지하수의 감소가 증가하고 있다. In Korea, it is difficult to secure stable water resources due to severe rainfall changes according to regions and seasons. In addition, with the rapid increase of urban use and industrialization, the increase of water usage, decrease of green area, and increase of the impermeable layer area such as concrete and asphalt have led to the decrease of groundwater.
따라서 사용하고 버려지는 오수, 폐수, 공정수 등을 처리하여 반복적으로 재 사용해야 하며, 이러한 수질오염 방지와 수자원의 안정적이고 경제적인 확보를 위하여, 오염도가 낮은 하수를 경제적으로 재처리하여 청소나 조경, 화장실 등의 용수로 정화하고, 재활용하는 중수도 시스템이 최대의 관심사가 되고 있다. 중수도의 수질은 물론 깨끗할수록 좋지만 처리 비용을 고려하여 용도에 맞게 적당한 수질로 만드는 것이 중요하다. 수질 목표는 사용자의 건강을 보호하고, 쾌적한 이용과 안정성을 확보하는 것이며, 이를 위해 다음과 같은 기본적인 사항이 검토되어야 하고 위생상의 문제점이 없어야 한다. 또한 이용 면에서 지장이 없어야 하고, 불쾌감을 주지 않아야 하며, 시설이나 기구에 악영향을 미치지 않아야 한다. 그리고 처리기술에 대한 안정성이 확립되어 있어야 하고, 유지관리 수준의 확보 및 판정을 위한 적절한 지표가 있어야 한다.Therefore, sewage, waste water, and process water that are used and discarded should be treated and reused repeatedly.In order to prevent water pollution and ensure stable and economical water resources, it is possible to economically reprocess sewage with low pollution to clean, landscaping, The biggest concern is the water-sewer system that purifies and recycles water from toilets and the like. Although the quality of the water is clean, the better it is, but it is important to make the water quality suitable for the purpose considering the treatment cost. The goal of water quality is to protect the user's health, to ensure pleasant use and stability, and the following basic matters should be reviewed and there should be no hygiene problems. In addition, there should be no inconvenience in use, no discomfort, and no adverse effect on the facility or apparatus. In addition, stability of treatment technology should be established and appropriate indicators for securing and determining maintenance levels.
일반적으로 오·하수를 처리하는 수처리 기술로는 응집, 침전, 분리, 흡착, 이온교환, 산화 등의 단위공정을 가지는 물리화학적 처리, 호기적 처리, 혐기적 처리, 동식물이나 미생물에 의한 생물학적 처리 및 상기 물리화학적 처리와 생물학적 처리공정을 단위공정으로 하여 조합하고 연계하여 처리하는 다단계처리가 개발되고 있다. 통상의 스크린 여과, 약품투입에 의한 응집, 침전처리, 활성탄 여과 등의 방법만으로는 운전비용이 많이 소요되고, 효율적인 정수처리가 되지 못하여 처리수질이 양호하지 못하다. 활성 슬러지를 이용한 생물학적 처리는 넓은 처리공간이 필요하고, 처리에 장시간이 소요됨은 물론 전문적인 관리가 필요하며, 처리비용이 과다한 문제점이 있다. 종래의 물의 안정성을 확보하기 위한 살균처리로 또한, 수중에 염소나 항생제 등을 투여하는 방법이 있으나, 이는 살균작용은 하지만 수중에 소독 제가 잔존하고 다른 화합물과 반응하여 2차 오염을 유발하게 되어 살균 후 안정성에 문제가 있다. Generally, water treatment technologies for treating sewage and sewage include physicochemical treatment, aerobic treatment, anaerobic treatment, biological treatment by animals and plants or microorganisms having unit processes such as flocculation, sedimentation, separation, adsorption, ion exchange, and oxidation. Multi-stage treatments have been developed in which the physicochemical treatment and biological treatment processes are combined as a unit process and processed in conjunction with each other. Normal screen filtration, agglomeration by chemical injection, sedimentation treatment, activated carbon filtration, etc. alone require a lot of operating costs, and it is not efficient water treatment, and the treated water quality is not good. Biological treatment using activated sludge requires a large treatment space, takes a long time to treatment, as well as professional management, there is a problem of excessive treatment costs. As a conventional sterilization treatment to ensure the stability of water, there is also a method of administering chlorine or antibiotics in water, but this is a sterilization action, but the disinfectant remains in water and reacts with other compounds to cause secondary pollution. There is a problem with stability after.
기존의 기술을 보면 1차적으로 부유물질과 탁도를 처리하기 위해 우리나라와 외국에서 사용하고 있는 여과기로 가장 많이 사용하였던 사여과는 모래와 작은 자갈을 이용하여 부유물질과 탁도, 색도을 제거하였는데 유지보수 및 처리효율이 떨어져 현재 다른 여과기로 대체 중이며, 아쿠아 디스크필터 여과기는 유입수질 및 유량변동에 따른 개별기기의 대처가 어려우며 디스크 세척시 고압사용으로 인한 엘러멘트의 수명감소와 파손우려가 있다. 또한 마이크로 디스크필터는 단일구동방식를 포함하지 않으므로 본체 및 부속설비의 고장시 처리가 불가하며, 중력식 자동역세 사여과지는 소유면적이 대단히 크고 초기 투자비가 많으며 역세수량이 많아 반송부하에 영향을 미치며 재처리 비용이 증가되는 문제점이 있다. 수지압착식 또한 소요면적이 비교적 크고, 여재의 량이 비교적 많고, 역세수량이 많아 반송부하에 영향을 미치며 재처리비용이 증가되는 문제점이 있다.According to the existing technology, the most commonly used filter for treating suspended solids and turbidity in Korea and foreign countries is the filtrate, which removes suspended solids, turbidity, and color using sand and small gravel. Due to the poor treatment efficiency, it is currently being replaced by another filter. Aqua disk filter filter is difficult to cope with individual equipments due to inflow water quality and flow rate change. In addition, the micro-disc filter does not include a single drive method, so it is impossible to deal with the failure of the main body and its accessories.The gravity automatic backwash filter has a very large possession area, a high initial investment cost, and a large amount of backwash water, which affects the return load. There is a problem that the cost is increased. The resin crimping type also has a relatively large required area, a relatively large amount of media, and a large amount of backwashing water, which affects the conveyance load and increases the reprocessing cost.
통상적으로 2차 처리 공정인 침지형 자외선 소독 장치 시스템은 수중에 수평으로 설비하는 수로형 타입과 챔버 관에 수직 또는 수평으로 설비하는 관로형 타입이 사용되어 왔다. 이는 별도의 수조를 만들거나 또는 관로형 자외선 장치를 위한 공간이 필요한 문제점이 있었다. The submerged UV disinfection device system, which is usually a secondary treatment process, has been used with a water channel type installed horizontally in water and a pipe type installed vertically or horizontally with a chamber tube. This is a problem that requires a separate tank or space for the pipeline UV device.
이에 본 발명자들은, 침지형 섬유여과기 및 침지형 자외선 장치를 여과소독방류조 내부에 일체로 설치하면, 협소한 공간에서도 방류수를 효율적으로 처리하여 중수 및 조경수로 재활용할 수 있음을 확인하고, 본 발명을 완성하게 되었다. Accordingly, the present inventors confirmed that, when the immersion type fiber filter and the immersion type UV device are integrally installed inside the filtration disinfection tank, the effluent can be efficiently treated in a narrow space and recycled into heavy water and landscape water, thereby completing the present invention. Was done.
본 발명의 목적은 협소한 장소에서도 설치가 용이하며, 효율적으로 방류수를 처리하여 중수 및 조경수로 재활용할 수 방류수 처리시스템 및 이를 이용한 방류수 의 처리방법을 제공하는데 있다. An object of the present invention is to provide a effluent treatment system and a method of treating effluent using the same, which can be easily installed even in a narrow place, and can be efficiently recycled to heavy water and landscape water by treating the effluent.
상기 목적을 달성하기 위하여, 본 발명은 유량조정조, 무산소조, 호기조, 침전조, 슬러지 저류조 및 여과소독방류조를 구비하는 방류수 처리시스템에 있어서, 상기 여과소독방류조의 내부에 침지형 섬유여과기 및 상기 침지형 여과기에서 여과된 방류수를 살균처리하는 침지형 자외선 소독장치가 설치된 것을 특징으로 하는 일체형 방류수 처리시스템을 제공한다.In order to achieve the above object, the present invention is a discharge water treatment system comprising a flow rate adjustment tank, an anoxic tank, an aerobic tank, a sedimentation tank, a sludge storage tank and a filtration disinfection tank, in the immersion type fiber filter and the immersion filter inside the filtration disinfection tank It provides an integrated effluent treatment system, characterized in that the immersion type ultraviolet disinfection device for sterilizing the filtered effluent water is installed.
본 발명은 또한, 상기 일체형 방류수 처리시스템을 이용하는 것을 특징으로 하는 방류수의 처리방법을 제공한다.The present invention also provides a method for treating effluent water, wherein the integrated effluent treatment system is used.
본 발명에 따른 일체형 방류수 처리시스템은 여과소독방류조 내부에 침지형 섬유여과기 및 침지형 자외선 소독장치가 설치되기 때문에, 별도의 공간이 필요 없이, 협소한 장소에도 용이하게 설치할 수 있다. 따라서, 이를 소규모 마을하수처리 장에 설치할 경우, 방류수를 중수 및 조경수로 재활용하는데 유용할 뿐만 아니라, 경제적으로도 바람직하다.In the integrated effluent treatment system according to the present invention, since an immersion type fiber filter and an immersion type UV disinfection device are installed in the filtration disinfection tank, it can be easily installed even in a narrow place without a separate space. Therefore, when it is installed in a small village sewage treatment plant, it is not only useful for recycling effluent to heavy water and landscape water, but also economically desirable.
본 발명은 일관점에서, 유량조정조(30), 무산소조(40), 호기조(50), 침전조(60), 슬러지 저류조(70) 및 여과소독방류조(80)를 구비하는 방류수 처리시스템에 있어서, 상기 여과소독방류조(80)의 내부에 침지형 섬유여과기(2) 및 상기 침지형 여과기(2)에서 여과된 방류수를 살균처리하는 침지형 자외선 소독장치(1)가 설치된 것을 특징으로 하는 일체형 방류수 처리시스템(100)에 관한 것이다.The present invention provides a discharge water treatment system including a flow
도 1에 나타난 바와 같이, 본 발명에 따른 방류수 처리시스템(100)은 통상적인 방류수 처리시스템과 같이, 유량조정조(30), 무산소조(40), 호기조(50), 침전조(60), 슬러지 저류조(70) 및 여과소독방류조(80)를 구비할 수 있다. 하지만, 본 발명에 따른 방류수 처리시스템(100)은 상기 여과소독방류조(80)의 내부에 침지형 섬유여과기(2) 및 상기 침지형 섬유여과기(2)에서 여과된 방류수를 살균처리하는 침지형 자외선 소독장치(1)가 설치된 것을 특징으로 한다.As shown in Figure 1, the
도 2는 침지형 섬유여과기 및 침지형 자외선 소독장치의 상세한 구조를 도시한 것이다.Figure 2 shows a detailed structure of the immersion type fiber filter and immersion type ultraviolet disinfection device.
본 발명에서 사용되는 침지형 섬유여과기는 방류수를 여과할 수 있는 것이라면 제한없이 사용될 수 있으나, 본 출원인의 한국등록특허(제10-0555055호)에 개시 된 침지형 섬유여과기를 사용하는 것이 바람직하다. The submerged fiber filter used in the present invention may be used without limitation as long as it can filter the effluent, but it is preferable to use the submerged fiber filter disclosed in the Korean Patent No. 10-0555055.
상기 침지형 섬유여과기는 관형 몸체에 부착된 광촉매 코팅 섬유 여과필터, 상기 섬유 여과필터의 관형 몸체를 회전시켜 섬유를 인장시키는 동력전달장치인 감속기 및 상기 감속기의 회전속도를 조절하는 인버터를 구비하는 것을 특징으로 한다. 즉, 상기 침지형 섬유여과기(2)는 광촉매 섬유여과필터를 이용할 수 있으며, 상기 광촉매 섬유여과필터는 광촉매(c-zon78-1, 엔비넷, 한국)를 코팅한 것으로 여과소독방류조 내부의 수중에 침지되어 설치된 구조이며, 탱크의 상부에는 섬유를 밀집시키는 동력전달장치인 감속기가 부착되어 있으며, 인버터가 오른쪽 왼쪽으로 섬유여과필터의 섬유를 인장시킬 수 있는 구조이다. 상기 감속기는 섬유여과필터의 베벨기어와 연결되어 있으며, 인버터가 감속기의 속도를 조절제어할 수 있도록 되어 있다. 상기 침지형 섬유여과기의 하부에 공기로 세척하기 위한 산기관을 포함하되, 산기관에서 발생하는 공기와 상기 침지형 섬유여과기(2)의 공극이 수직으로 접촉하도록 구성되어 있다. The submerged fiber filter includes a photocatalyst coated fiber filtration filter attached to the tubular body, a speed reducer which is a power transmission device for tensioning the fiber by rotating the tubular body of the fiber filtration filter, and an inverter for controlling the rotation speed of the reducer. It is done. That is, the submerged fiber filter 2 may use a photocatalyst fibrous filter, and the photocatalyst fibrous filter is coated with a photocatalyst (c-zon78-1, Envinet, Korea) in the water inside the filtration tank. It is a structure that is immersed and installed, and the upper part of the tank is attached to a speed reducer, which is a power transmission device for dense fibers, and the inverter is able to tension the fibers of the fiber filtration filter to the right and left. The speed reducer is connected to the bevel gear of the fiber filtration filter, and the inverter is capable of regulating and controlling the speed of the speed reducer. Included in the lower part of the submerged fiber filter for washing with air, the air generated in the diffuser is configured to vertically contact the air gap of the submerged fiber filter (2).
본 발명에 따른 침지형 섬유여과기는 중공관, 한 방향 베어링이 삽입되어 있고 섬유모듈이 부착되어있는 구조인 하우징, 광촉매섬유의 양끝에 섬유다발을 고정하는 연결고리, 축, 중공관 모듈을 지지하는 브라켓, 광촉매가 코팅된 섬유여과필터, 광촉매가 코팅되어 있는 테프론 재질의 섬유, 동력전달을 하는 베벨기어(메인기어), 메인기어의 동력을 전달받는 구조의 베벨기어(로컬기어), 섬유의 인장 및 회전 속도를 조절하는 인버터, 동력전달장치인 감속기, 감속기 축과 베벨기어 축의 연결부인 커플링, 관형의 몸체에 에어분산 모듈이 붙어있는 구조인 산기관, 관형의 수로, 슬러리 배출 배관, 스케일이 생기면 슬러리를 배출하는 수로 등으로 구성되어 있다.The submerged fiber filter according to the present invention is a hollow tube, a housing in which one-way bearing is inserted and a fiber module is attached, a connecting ring for fixing the fiber bundle at both ends of the photocatalytic fiber, a shaft, and a bracket for supporting the hollow tube module. , Fiber filtration filter coated with photocatalyst, Teflon fiber coated with photocatalyst, bevel gear (main gear) for power transmission, bevel gear (local gear) for receiving power from main gear, tension of fiber and Inverter to control rotation speed, reducer as power transmission device, coupling as connection between reducer shaft and bevel gear shaft, diffuser structure with air dispersion module attached to tubular body, tubular channel, slurry discharge pipe, scale It consists of a channel etc. which discharge | release a slurry.
또한, 본 발명에 따른 상기 침지형 섬유여과기(2)는 상기 여과소독방류조 바닥에 설치된 300~500mm 높이의 방류수조 플레임(5) 상부에 위치하는 것을 특징으로 한다. 따라서, 비중이 있는 슬러지 및 이물질(SS)들은 바닥으로 침전되며, 바닥에 농축된 슬러지는 에어펌프(21)를 통하여 슬러지저류조로 이송되기 때문에, 본 발명에 따른 방류수 처리시스템(100)은 효율적으로 방류수를 여과할 수 있는 장점이 있다.In addition, the immersed fiber filter (2) according to the invention is characterized in that it is located on the discharge tank flame 5 of the 300 ~ 500mm height installed on the bottom of the filter sterilization discharge tank. Therefore, the sludge and foreign matter (SS) having a specific gravity is settled to the bottom, since the sludge concentrated on the bottom is transferred to the sludge storage tank through the air pump 21, the
본 발명에 따른 상기 침지형 섬유여과기(2)는 일정한 레벨을 유지하는 레벨제어, 필터의 이물질 분리제거를 위한 세척, 오염된 배관의 세척, 연속운전 등의 과정을 거치며 작동될 수 있다.The submerged fiber filter 2 according to the present invention can be operated through a process such as level control to maintain a constant level, washing for separation and removal of foreign matter in the filter, washing of contaminated pipe, continuous operation.
상기 레벨제어의 방법을 살펴보면, 방류수조의 수위가 LOW LEVEL(17)일때 펌프(7)는 정지되어서 방류수조의 최저수위를 유지하고, 일정한 시간이 지나면서 수위가 MID LEVEL(18) 및 Hi LEVEL(19)이 되면 펌프(7)가 가동되어 수위를 떨어지게 한다. Hi LEVEL(19)에서는 큰 밸브(10)가 열려있어 배관의 유량이 많이 흐르고 수위는 떨어진다. 수위가 계속 떨어져서 MID LEVEL(18)이 되면 큰 밸브(10)는 잠기고, 작은 밸브(9)가 열려서 배관의 유량이 큰 밸브가 열렸을 때보다 감소되어 수위는 조금씩 떨어진다. 이때 Hi LEVEL(19)에서 Low LEVEL(17)까지 떨어지는데 2시간 이상 시간이 걸리는 것이 운영하기 좋다. Looking at the level control method, when the water level of the discharge tank is LOW LEVEL (17), the pump (7) is stopped to maintain the minimum level of the discharge tank, and the water level is MID LEVEL (18) and Hi LEVEL (19) after a certain period of time. ), The pump (7) starts to drop the water level. In the Hi LEVEL 19, the
침지형 섬유여과기(2)의 효율이 떨어져 배수구의 유량이 점점 줄어들었을 때 여과기의 필터를 역회전시키는 세척시기를 결정하는 것은 제어판넬의 HMI(Human Machine Interface) 프로그램에 의해 제어될 수 있다. 즉, Hi LEVEL(19)에서 MID LEVEL(18)를 거쳐 Low LEVEL(17)로 수위가 떨어지는 것을 HMI에서 측정해서 50%정도의 효율이 떨어졌을 때 침지형 섬유여과기의 필터를 역회전시켜 이물질을 세척할 수 있다. 하수처리장의 물 처리의 효율에 따라서 여과기의 세척주기는 조절할 수 있다. Determining when to flush the filter of the filter back when the efficiency of the submerged fiber filter 2 decreases and the flow rate of the drain is gradually reduced can be controlled by the Human Machine Interface (HMI) program of the control panel. In other words, when the water level drops from Hi LEVEL (19) to MID LEVEL (18) to Low LEVEL (17) and the level is reduced by about 50%, the filter of the immersion type fiber filter is rotated in reverse to wash foreign substances. Can be. The washing cycle of the filter can be adjusted according to the efficiency of water treatment in the sewage treatment plant.
여과기의 필터 세척 후, 부유물질들이 필터 안으로 들어와 일부 배관을 오염시킬 수 있다. 따라서 배관에 있는 오염된 물을 리턴밸브(8)를 열어서 슬러지저류조로 1분 이상 배수시킨다. 그리고 리턴밸브(8)를 닫고 큰 밸브(10)를 열어서 계속 공정을 진행시킨다.After cleaning the filter in the strainer, suspended solids can enter the filter and contaminate some piping. Therefore, the contaminated water in the pipe is drained to the sludge storage tank by opening the return valve 8 for at least 1 minute. Then, the return valve 8 is closed and the
배수용 펌프(7)는 여과기의 상부에 위치한 펌프베이스(11)에 설치되어 있고, 펌프가 정지되었을때 역류 방지를 위해 체크밸브(22) 유입구에 설치되어있다. 상기 펌프베이스(11)는 커버 및 배수구(12)가 있어 베이스바닥의 청결을 유지할 수 있다. 필터링된 깨끗한 방류수는 미생물의 살균을 위해 침지형 자외선 소독장치(1)로 펌핑된다.The drain pump 7 is installed at the pump base 11 located at the top of the filter, and is installed at the check valve 22 inlet to prevent backflow when the pump is stopped. The pump base 11 has a cover and a drain 12 to maintain the base floor clean. The filtered clean effluent is pumped into an immersion type ultraviolet disinfection device 1 for the sterilization of microorganisms.
본 발명에 따른 일체형 방류수 처리시스템의 침지형 자외선 소독장치(1)는 통상적인 것을 제한없이 사용할 수 있으나, 상기 섬유여과기(2)에서 여과된 방류수가 유입되는 U자형관(3) 및 여과소독된 방류수가 배출되도록 상기 여과소독방류조(80)의 일벽면을 관통하며 설치되어 있는 방류수배관(4)에 각각 연결된 것을 사 용하는 것이 바람직하다. 즉, 본 발명에 따른 침지형 자외선 소독장치(1)는 상기 U자형관(3) 및 상기 방류수배관(4)의 중간에 위치한다. Immersion type ultraviolet disinfection device (1) of the integrated effluent treatment system according to the present invention can be used without limitation, the U-shaped tube (3) and filtered sterilized effluent flowing in the effluent filtered in the fiber filter (2) It is preferable to use each connected to the discharge water pipe (4) which is installed penetrating through the one wall surface of the filtration disinfection and discharging tank (80) so as to discharge. That is, the immersion type ultraviolet disinfection device 1 according to the present invention is located in the middle of the U-shaped pipe 3 and the discharge water pipe 4.
상기 침지형 자외선 소독장치(1)는 자외선 램프(16)의 효율 유지를 위한 세척장치(14)가 부착된 것이 바람직하며, 상기 자외선 램프(16)는 석영관에 삽입된 구조이며, 침수시 실링이 되도록 오링구조의 캡이 상부에 나사타입으로 막혀져 있으며, 배선은 튜브 속에 있어 실링이 된 것을 사용하는 것이 바람직하다. The immersion type ultraviolet disinfection device (1) is preferably attached to the cleaning device 14 for maintaining the efficiency of the ultraviolet lamp 16, the ultraviolet lamp 16 is a structure inserted into the quartz tube, when the immersion sealing If possible, the cap of the O-ring structure is clogged with a screw type at the top, and it is preferable to use the sealed wire in the tube.
본 발명은 다른 관점에서, 상기 일체형 방류수 처리시스템을 이용하는 것을 특징으로 하는 방류수의 처리방법에 관한 것이다. In another aspect, the present invention relates to a method for treating effluent water, wherein the integrated effluent treatment system is used.
본 발명에 있어서, 방류수 처리시스템의 운영은 컴퓨터에 의한 자동 운영방식으로 온도, 레벨, 유량제어, 동력제어 및 산화량을 제어할 수 있는 통합관리방식의 HMI(Human Machine Interface) 구조인 것이 바람직하다. In the present invention, the operation of the effluent treatment system is preferably an HMI (Human Machine Interface) structure of an integrated management method that can control the temperature, level, flow control, power control and oxidation amount by an automatic operation method by a computer. .
이상으로 본 발명의 특정한 부분을 상세히 기술하였는바, 당업계의 통상의 지식을 가진 자에게 있어서, 이러한 구체적 기술은 단지 바람직한 실시양태일 뿐이며, 이에 의해 본 발명의 범위가 제한되는 것은 아닌 점은 명백할 것이다. 따라서 본 발명의 실질적인 범위는 첨부된 청구항들과 그것들의 등가물에 의하여 정의된다고 할 것이다. Having described the specific parts of the present invention in detail, it will be apparent to those skilled in the art that such specific descriptions are merely preferred embodiments, and thus the scope of the present invention is not limited thereto. will be. Thus, the substantial scope of the present invention will be defined by the appended claims and their equivalents.
도 1은 침지형 섬유여과기 및 침지형 자외선 소독장치를 방류조에 일체형으로 설치한 방류수 처리시스템의 공정도를 도시한 것이다.1 shows a process diagram of a effluent treatment system in which an immersion type fiber filter and an immersion type ultraviolet disinfection device are integrally installed in a discharge tank.
도 2는 침지형 섬유여과기 및 침지형 자외선 소독장치의 상세한 구조를 도시한 것이다.Figure 2 shows a detailed structure of the immersion type fiber filter and immersion type ultraviolet disinfection device.
<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>
1: 침지형 자외선 소독장치 2: 침지형 섬유여과기1: immersion type ultraviolet disinfection device 2: immersion type fiber filter
3: U자형관 4: 방류수배관3: U-shaped pipe 4: discharge pipe
5: 플레임 6: 감속기5: flame 6: reducer
7: 펌프 8: 리턴밸브7: Pump 8: Return Valve
9: 작은 밸브 10: 큰 밸브9: small valve 10: large valve
11: 펌프베이스 12: 배수구 11: pump base 12: drain
13: 플랜지 14: 세척장치13: flange 14: cleaning device
15: 방류수 유입구 16: 자외선 램프 15: effluent inlet 16: ultraviolet lamp
17: LOW LEVEL 18: MID LEVEL 17: LOW LEVEL 18: MID LEVEL
19: Hi LEVEL 20: HiHi LEVEL19: Hi LEVEL 20: HiHi LEVEL
21: 에어펌프 22: 체크밸브21: air pump 22: check valve
30: 유량조정조 40: 무산소조30: flow adjustment tank 40: anoxic tank
50: 호기조 60: 침전조50: aeration tank 60: sedimentation tank
70: 슬러지 저류조 80: 여과소독방류조 70: sludge storage tank 80: filtered sterilization discharge tank
100: 방류수 처리시스템100: effluent treatment system
Claims (7)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020080036820A KR20090111188A (en) | 2008-04-21 | 2008-04-21 | Discharged Water Treatment System and Method for Treating Discharged Water Using the Same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020080036820A KR20090111188A (en) | 2008-04-21 | 2008-04-21 | Discharged Water Treatment System and Method for Treating Discharged Water Using the Same |
Publications (1)
Publication Number | Publication Date |
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KR20090111188A true KR20090111188A (en) | 2009-10-26 |
Family
ID=41538974
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020080036820A KR20090111188A (en) | 2008-04-21 | 2008-04-21 | Discharged Water Treatment System and Method for Treating Discharged Water Using the Same |
Country Status (1)
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KR (1) | KR20090111188A (en) |
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KR101236004B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Submerged MBR system comprising U―form inline mixer |
KR101236029B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Method for controlling submerged MBR system |
WO2014137026A1 (en) * | 2013-03-06 | 2014-09-12 | 주식회사 세기종합환경 | Water treatment apparatus |
CN108524996A (en) * | 2018-04-17 | 2018-09-14 | 上海海事大学 | A kind of device for inhibiting marine aluminium alloy to corrode in process |
CN108706796A (en) * | 2018-05-29 | 2018-10-26 | 宿州冬宇环保科技有限公司 | A kind of electroplating waste processing process |
CN113683238A (en) * | 2021-08-26 | 2021-11-23 | 生态环境部南京环境科学研究所 | Recirculating aquaculture water treatment system and treatment method thereof |
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2008
- 2008-04-21 KR KR1020080036820A patent/KR20090111188A/en not_active Application Discontinuation
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101236004B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Submerged MBR system comprising U―form inline mixer |
KR101236029B1 (en) * | 2011-03-09 | 2013-02-21 | 주식회사 동양 | Method for controlling submerged MBR system |
WO2014137026A1 (en) * | 2013-03-06 | 2014-09-12 | 주식회사 세기종합환경 | Water treatment apparatus |
CN108524996A (en) * | 2018-04-17 | 2018-09-14 | 上海海事大学 | A kind of device for inhibiting marine aluminium alloy to corrode in process |
CN108706796A (en) * | 2018-05-29 | 2018-10-26 | 宿州冬宇环保科技有限公司 | A kind of electroplating waste processing process |
CN108706796B (en) * | 2018-05-29 | 2020-07-24 | 泰州市龙沟电镀科技有限公司 | Electroplating wastewater treatment process |
CN113683238A (en) * | 2021-08-26 | 2021-11-23 | 生态环境部南京环境科学研究所 | Recirculating aquaculture water treatment system and treatment method thereof |
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