KR20000009525A - General waste water treatment system - Google Patents
General waste water treatment system Download PDFInfo
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- KR20000009525A KR20000009525A KR1019980030007A KR19980030007A KR20000009525A KR 20000009525 A KR20000009525 A KR 20000009525A KR 1019980030007 A KR1019980030007 A KR 1019980030007A KR 19980030007 A KR19980030007 A KR 19980030007A KR 20000009525 A KR20000009525 A KR 20000009525A
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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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
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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
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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
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- 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)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
본 발명은 일반 페수 처리 시스템에 관한 것으로서, 더욱 상세하게는 폐수 처리를 함에 있어서, 많은 양의 폐수를 신속히 처리할 수 있으며 각각의 다단계 공정을 거친 폐수를 저장하기 위한 저장조가 필요치 않으며, 이러한 것을 하나의 가압 탱크에서 처리케 하여 시스템 유지비가 저렴하게 들게 한 일반폐수 처리 시스템에 관한 것이다.The present invention relates to a general wastewater treatment system, and more particularly, in the treatment of wastewater, it is possible to quickly treat a large amount of wastewater and does not require a reservoir for storing wastewater after each multi-step process. The present invention relates to a general wastewater treatment system which is treated in a pressurized tank, thereby making the system maintenance cost low.
종래의 경우, 폐수 처리 시스템이라 하면, 도 3에서 보는 바와 같이 폐수를 반응조, 응집 교반조, 그리고, 응집 활성조로 순차 흘러 들게 되면서, 각각 반응제(NaOH), 응집제(ALUM), 응집보조제(Polymer), 등의 약품을 첨가하고, 이는 가압 탱크로 흘러 들어가서 에어와 펌프압에 의해서 물에 용해되어서, 압력에 의해 응집된 상태로 부상조로 공급되게 하면, 부상조에서는 수면위로 떠오르는 각종 슬러지를 제거하여, 폐수를 정화하는 시스템으로 이루어져 있었다.In the conventional case, the wastewater treatment system, as shown in FIG. 3, flows the wastewater into the reaction tank, the coagulation stirring tank, and the coagulation activating tank sequentially, respectively, and reactants (NaOH), coagulant (ALUM), and coagulant aid (Polymer), respectively. Chemicals, etc., which flows into the pressurized tank, is dissolved in water by air and pump pressure, and supplied to the flotation tank in a flocculated state by the pressure, and the flotation tank removes the various sludges that float on the water surface. The system consisted of a system for purifying wastewater.
그러나 이와 같은 종래의 기술은 각각의 저장조에 의해 그 크기와 용량이 많은 면적을 차지하게 되었고, 이로 인해 많은 폐수를 효율적으로 처리하지 못하는 문제점이 있었다.However, such a conventional technology is occupied a large area of the size and capacity by each storage tank, there is a problem that does not efficiently treat a large amount of waste water.
따라서 본 발명은 상술한 바와 같은 종래 기술의 제반 문제점을 감안하여 안출된 것으로서, 다량의 폐수를 단시간에 정수 처리 할 수 있게 하면서, 종래 기술에 비해 응집, 반응조가 필요하지 않으며, 또한, 다량의 약품주입 및 과대한 시설에 대한 설치면적을 간소화시킬 수 있고, 폐수의 체류 시간이 단축되어, 변화 폭이 큰 수질에 대하여 신속히 반응할 수 있게 한 일반 폐수 처리 시스템을 제공하는데 그 목적이 있는 것이다.Therefore, the present invention has been devised in view of the above-mentioned problems of the prior art, and enables a large amount of wastewater to be purified in a short time, and does not require agglomeration and a reaction tank compared to the prior art, and also requires a large amount of chemicals. It is an object of the present invention to provide a general wastewater treatment system which can simplify the installation area of the injection and oversize facilities, and shorten the residence time of the wastewater, thereby enabling a rapid response to a large change in water quality.
도 1은 본 발명의 페수 처리 시스템에 대한 구성도1 is a block diagram of a wastewater treatment system of the present invention
도 2는 본 발명의 페수 처리 시스템에 대한 공정도2 is a process chart for the wastewater treatment system of the present invention.
도 3은 종래 기술에 폐수 처리 시스템에 대한 구성도3 is a block diagram of a wastewater treatment system in the prior art
(도면의 주요부분에 대한 부호의 설명)(Explanation of symbols for the main parts of the drawing)
10...,폐수 저장조 11...,폐수 공급 펌프 12...,가압탱크10 ..., wastewater reservoir 11 ..., wastewater supply pump 12 ..., pressurized tank
13...,보조탱크 14...,가압 부상기 15...,공기 압축기13 ..., auxiliary tank 14 ..., pressurized floater 15 ..., air compressor
16...,슬러지 분리기 17...,슬러지 저장조 18...,1차 정화수 저장조16 ..., sludge separator 17 ..., sludge reservoir 18 ..., primary septic tank
19...,마이크로백 필터 20...,카본 필터 21...,마이크로 필터19 ..., Microbag Filter 20 ..., Carbon Filter 21 ..., Micro Filter
22...,역삼투압막 23...,약품탱크 24...,희석용 정수 탱크22 ..., reverse osmosis membrane 23 ..., chemical tank 24 ..., dilution water purification tank
25...,약품주입펌프 26...,처리대상수 저장조 27...,최종 정화수 저장조25 ..., chemical injection pump 26 ..., treated water reservoir 27 ..., final purified water reservoir
28...,탈수기28 ..., dehydrator
이하 첨부된 도면을 참조하여 본 발명의 목적을 달성하기 위한 기술적 구성 및 작용 효과를 상세히 설명하면 다음과 같다.Hereinafter, with reference to the accompanying drawings will be described in detail the technical configuration and effect for achieving the object of the present invention.
도 1은 본 발명의 시스템 구성도에 관한 것으로서, 참조부호 10은 폐수 유입관을 통해 일정 양 저장되는 폐수 저장조이고, 11은 폐수 저장조에 저장된 폐수를 펌핑으로 끌어 올려 가압탱크에 공급하는 폐수 공급펌프 이고, 12는 공급 된 원 폐수를 직접 가압 하는 가압탱크, 13은 가압탱크에서 미처 처리하지 못하는 폐수를 처리하는 가압 보조 탱크, 14는 고압의 압에 의해 폐수와 약품 그리고 용해된 공기가 주입되면서, 슬러지 등이 수면으로 뜨게 하는 가압 부상기,1 is a system configuration diagram of the present invention, reference numeral 10 is a wastewater storage tank which is stored in a predetermined amount through the wastewater inlet pipe, and 11 is a wastewater supply pump for drawing up the wastewater stored in the wastewater storage tank by pumping and supplying it to the pressure tank. 12 is a pressurized tank for directly pressurizing the supplied raw wastewater, 13 is a pressurized auxiliary tank for treating wastewater that cannot be treated in the pressurized tank, and 14 is injected with wastewater, chemicals and dissolved air by high pressure. Pressurized injuries that cause sludge to float to the surface,
15는 에어를 압축하여 이를 가압탱크에 공급하여 폐수에 압축된 고압의 공기를 주입시켜 폐수에 공기를 용해시키는 공기 압축기이고, 16은 페수 저장조의 슬러지를 1차로 걸러내는 슬러지 분리기, 17은 가압 부상기를 통해 배출되는 슬러지를 저장하는 슬러지 탱크이다.15 is an air compressor that compresses air and supplies it to a pressurized tank to inject compressed air into the wastewater to dissolve the air in the wastewater. 16 is a sludge separator that first filters sludge from the wastewater storage tank, and 17 is a pressurized flotation. Sludge tank to store the sludge discharged through the machine.
그리고, 18은 가압부상기를 통해 1차 정수된 정화수를 저장하는 1차 정화수 저장조 이며, 19는 마이크로 백 필터 20은 카본 필터, 21은 마이크로 필터 22는 역삼투압막이다.In addition, 18 is a primary purified water storage tank for storing the purified water primary through the pressurization, 19 is a micro bag filter 20 is a carbon filter, 21 is a micro-filter 22 is a reverse osmosis membrane.
또한, 23은 반응제(ALUM), 응집제(NaOH), 응집 보조제(polymer)등의 약품을 저장하는 약품 탱크이고, 24는 희석용 정수를 보관하는 탱크, 25는 순환펌프 26은 모든 과정을 통과한 상태의 처리대상수 저장조, 27은 최종 처리 과정이 완료된 상태의 정화수를 보관하는 정화수 탱크를 지칭하는 것이다.In addition, 23 is a chemical tank for storing chemicals such as ALUM, agglomerate (NaOH), and coagulation aid (polymer), 24 is a tank for storing purified water for dilution, and 25 is a circulation pump 26 for all processes. A treatment water storage tank in one state, 27 refers to a purification water tank that stores purified water in a state where the final treatment process is completed.
이상과 같이 구성되어진 본 발명의 작용 및 효과를 바람직한 실시 예에 의거하여 설명하면 다음과 같다.Referring to the operation and effect of the present invention configured as described above based on the preferred embodiment are as follows.
도 1에서 보는 바와 같이 폐수 유입관을 통해 유입되는 페수는 폐수저장조(10)에 보관되고, 일정 이상으로 저장된 폐수는 폐수공급펌프(11)의 가동으로 가압 탱크(12)에 공급되면서 1치적으로 폐수에 함유되어 있는 슬러지는 슬러지 분리기를 통해 걸러지며, 이때의 슬러지는 슬러지 저장탱크로 보내지고 슬러지를 제거한 상태의 원 페수는 가압탱크로 공급된다.As shown in FIG. 1, the wastewater flowing through the wastewater inlet pipe is stored in the wastewater storage tank 10, and the wastewater stored more than a predetermined time is supplied to the pressurized tank 12 by the operation of the wastewater supply pump 11. The sludge contained in the waste water is filtered through the sludge separator, and the sludge is sent to the sludge storage tank, and the raw waste water in which the sludge is removed is supplied to the pressurized tank.
가압탱크(12)에서는 원 페수를 직접가압(4∼8㎏/㎠) 하며, 공기압축기(21)에서 공급되는 고압의 공기가 공급되면서, 이는 폐수에 용해되면서 슬러지를 압력에 이해 응집되게 한다.In the pressurized tank 12, the raw wastewater is directly pressurized (4 to 8 kg / cm 2), while the high pressure air supplied from the air compressor 21 is supplied, which dissolves in the wastewater and causes the sludge to be aggregated under pressure.
이때, 가압탱크(12)를 거친 페수는 공급 라인(L)을 따라, 가압 부상기(14)에 공급되는데, 공급 라인(L)상에는 페수를 희석 되게 하거나, 강제 분리시키는 반응제(NaOH)와 응집제(Alum), 그리고 응집 보조제(POLYMER)가 투입된다.At this time, the wastewater passing through the pressure tank 12 is supplied to the pressure flotation 14 along the supply line (L), and the reactant (NaOH) for diluting or forcibly separating the wastewater on the supply line (L). Alum and POLYMER are added.
즉, 약품탱크에는 각각의 약품을 충진시키고, 가동되게 하면 교반동작이 이루어 진다.In other words, the medicine tank is filled with each medicine, and the operation is made to the stirring operation.
이어서, 약품탱크(23)에 저장된 약품은 순환펌프의 펌핑에 의해 보조 가압 탱크(13)에 공급되고, 보조 가압 탱크(13)에서는 일정압으로 교반되어, 상기 폐수 공급 라인(L)을 따라 약품이 공급되면서, 폐수와 섞이게 되어 반응이 일어나게 되는데, 이러한 약품은 보조 가압 탱크(13)에 유입되어, 물과 혼합 및 반응되고, 또 부상조의 처리수 60%를 재 순환하여, 가압 부상기(14) 내의 공기를 보충하여 주거나, 응집된 부유물의 비중이나 크기에 따라 부유물의 상승 속도를 조절하게 된다.Subsequently, the chemicals stored in the chemical tank 23 are supplied to the auxiliary pressurization tank 13 by pumping of the circulation pump, and the auxiliary pressurization tank 13 is stirred at a constant pressure, and the chemicals are supplied along the wastewater supply line L. While supplied, it is mixed with the waste water to cause a reaction, which is introduced into the auxiliary pressurized tank 13, mixed with and reacted with water, and recirculated 60% of the treated water in the flotation tank, thereby increasing the pressure flotation (14). ) To replenish air or adjust the rate of rise of the float according to the specific gravity or size of the flocculated float.
이어서 일정압으로 압축된 폐수는 가압 부상기(14)에 공급 될 때에 고압의 페수는 자연압으로 바뀌면서 공급되고, 약품에 의해 슬러지 등과 결착되어 유입구의 유체적 공급 라인 믹서에 주입이 되어 가압 부상기(14) 내에서 응집이 이루어 진다.Subsequently, when the wastewater compressed to a constant pressure is supplied to the pressure flotation 14, the high-pressure wastewater is supplied while changing to natural pressure, and is bound to sludge by chemicals and injected into the fluid supply line mixer at the inlet to pressurized flotation Agglomeration is achieved in (14).
이때, 응집된 슬러지 등은 가압 부상기(14)의 수면 위에 떠오르게 되는데, 실험에 의하면, 가압 부상기(14) 내의 부유물 부상속도는 1m-2m/분이 소요되며, 원 폐수 처리 시간은 1∼5분 정도가 소요되었다.At this time, the flocculated sludge or the like floats on the water surface of the pressurized flotation machine 14. According to the experiment, the float floating speed in the pressurized flotation machine 14 takes 1m-2m / min, and the original wastewater treatment time is 1-5. It took about a minute.
한편, 가압 부상기의(14) 상측부에 마련된 플로터에 의해, 슬러지가 제거되고 이는 슬러지 공급라인을 따라 슬러지 저장조(17)에 저장되는 것이다.On the other hand, by the plotter provided in the upper portion of the pressure floating body 14, sludge is removed, which is stored in the sludge storage tank 17 along the sludge supply line.
또한, 가압 부상기(40)에서 계속적으로 유입되는 페수에서 슬러지를 제거하고, 남은 폐수는 정수조(18)에 공급되면서 일정시간 경과후에 펌핑으로 마이크로 백 필터(19), 카본 필터(20), 마이크로 필터(21)를 순차적으로 거치면서 불순물을 완전 제거하고, 이때, 1차 정화된 폐수를 희석하는 정수가 저장되어 있는 희석용 정수 탱크(24)에 담겨 있는 물은 순환펌프(25)의 펌핑력에 의해 1차 정수 처리된 물과 섞이면서, 역삼투압막을 강제로 통과시켜 최종적인 정수처리를 수행하게 된다.In addition, the sludge is removed from the wastewater continuously flowing from the pressurized floater 40, and the remaining waste water is supplied to the water purification tank 18, and after a predetermined time, the micro bag filter 19, the carbon filter 20, Impurities are completely removed while sequentially passing through the micro filter 21. At this time, the water contained in the dilution purified water tank 24 in which the purified water for diluting the first purified wastewater is stored is pumped from the circulation pump 25. While mixing with the first purified water by force, the reverse osmosis membrane is forced through the final purified water treatment.
이어서, 모든 과정을 거친 정수는 침전조(26)에 저장되어 일정시간이 경과되면 최종적으로 정화수 저장조에 담겨지게 되고 이는 용도에 따라 방류되는 것이다.Subsequently, all the purified water is stored in the settling tank 26, and after a predetermined time is finally contained in the purified water storage tank is discharged according to the purpose.
이상에서 설명된 바와 같이 본 발명은, 폐수 처리 효과가 기존의 방식에 비해 뛰어나며, 유지비가 저렴하고, 별도의 응집, 반응조가 불필요하며, 면적이 작아 어느 곳에나 설치 할 수 있으며, 기존의 가압 부상 장치보다 획기적으로 개선한 새로운 차원의 발명인 것이다.As described above, the present invention, the waste water treatment effect is superior to the existing method, the maintenance cost is low, no need for separate agglomeration, reaction tank, small area can be installed anywhere, the existing pressure rise It's a new level of invention that's a major improvement over devices.
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KR100383802B1 (en) * | 2000-12-13 | 2003-05-12 | 정병욱 | Apparatus for clarifying raw water |
KR100399252B1 (en) * | 2001-06-12 | 2003-09-26 | 차원량 | A Handling Methods of the Kanari Waste |
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---|---|---|---|---|
JPS63209785A (en) * | 1987-02-27 | 1988-08-31 | Hitachi Plant Eng & Constr Co Ltd | Flocculating, pressurizing and floating apparatus |
JPH072446A (en) * | 1993-06-15 | 1995-01-06 | Hitachi Building Syst Eng & Service Co Ltd | Inspecting device for elevator display lamp |
-
1998
- 1998-07-25 KR KR1019980030007A patent/KR100302017B1/en not_active IP Right Cessation
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100383802B1 (en) * | 2000-12-13 | 2003-05-12 | 정병욱 | Apparatus for clarifying raw water |
KR100399252B1 (en) * | 2001-06-12 | 2003-09-26 | 차원량 | A Handling Methods of the Kanari Waste |
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KR100302017B1 (en) | 2001-11-30 |
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