KR20010048831A - height well water at its purest equipment - Google Patents
height well water at its purest equipment Download PDFInfo
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- KR20010048831A KR20010048831A KR1019990053654A KR19990053654A KR20010048831A KR 20010048831 A KR20010048831 A KR 20010048831A KR 1019990053654 A KR1019990053654 A KR 1019990053654A KR 19990053654 A KR19990053654 A KR 19990053654A KR 20010048831 A KR20010048831 A KR 20010048831A
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- biofilm
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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
- C02F3/06—Aerobic processes using submerged filters
-
- 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
Abstract
Description
본 발명은 생물막 여과에 의한 상수원수 전처리 및 고도 정수 장치에 관한 것으로 생물막 여과 전처리 공정과 후속 정수 공정인 생물막 활성탄 공정 BAC(오존+GAC) 또는 입상활성탄 공정(GAC)을 추가하여 양질의 수돗물을 생산할 수 있게 한 것이다.The present invention relates to a water purification pretreatment and advanced water purification apparatus by biofilm filtration, and to add a biofilm filtration pretreatment process and a subsequent biofilm activated carbon process BAC (ozone + GAC) or granular activated carbon process (GAC) to produce high quality tap water. It was made possible.
종래에 우리나라는 대부분 상수원을 하천, 호소 등의 지표수를 의존하고 있어 상수원수에 대한 수질오염이 심각한 국가적 문제가 되고 있다. 특히, 낙동강 하류부에 위치한 부산, 경남 지역의 상수원수 수질이 원수등급 4∼5급수로 악화되어 상수원수로 사용할 수 없는 상태에까지 이르고 있다.In the past, most of Korea relies on surface water such as rivers and lakes for drinking water, so water pollution to drinking water has become a serious national problem. In particular, the water quality of drinking water in Busan and Gyeongnam, which is located in the lower part of the Nakdong River, has deteriorated to grade 4 to 5 and has reached the state where it cannot be used as water supply.
이러한 상수원수를 개선하기 위해서 현재 전염소(Pre-Chlorination)처리 또는 전오존(Pre-Ozonation)처리 등을 수행하고 있으나 전자의 경우는 발암물질인 THMs발생, 후자의 경우는 암모니아성질소(NH4-N)가 제거되지 않는 등 근본적인 대책이 되지 못하고 있어 수돗물에 대한 불신이 점점 깊어지고 있다.In order to improve the water supply, pre-chlorination or pre-zonation treatment is currently performed, but in the former case, THMs, which are carcinogens, and in the latter case, ammonia nitrogen (NH 4 -N) has not been eliminated, such as not being removed, and the distrust of tap water is deepening.
오존과 입상활성탄(BAC)을 이용한 기존의 전오존과 고도정수시스템은 전오존처리 효과가 미흡하여 NH4-N가 거의 제거되지 않았으며 BOD, COD 등 각종 오염 물질의 제거율이 매우 낮아 원수 수질이 급격히 악화되는 상태에서는 BAC공정의 수명이 매우 짧은 시간내 파과상태가 이루어져 효과적인 정수처리가 어렵고 또 빈번한 역세나 BAC공정의 수명이 매우 단축되어 입상활성탄의 교체가 요구되어 매우 비경제적인 상수도 물이 생산될 수 밖에 없었다.Existing ozone and advanced water purification systems using ozone and granular activated carbon (BAC) have insufficient effect of ozone treatment and almost no NH 4 -N has been removed, and the removal rate of various pollutants such as BOD and COD is very low. In the rapidly deteriorating state, the life of the BAC process is broken in a very short time, which makes it difficult to effectively purify the water, and frequent backwashing or the life of the BAC process is very short, requiring the replacement of granular activated carbon. There was no choice but to.
기존의 급속여과시스템을 후속공정으로 할 경우 응집침전지와 급속 모래여과지 등 부지면적이 넓게 요구되며 응집약품이 다량 소모되고 슬러지 발생량이 과다하여 정수시스템 운전의 경비가 높아질수 밖에 없는 등의 폐단이 있었다.If the existing rapid filtration system is a follow-up process, the land area such as flocculation settler and rapid sand filtration paper is widely required, and the cost of running the water purification system is inevitably increased due to the large amount of flocculating chemicals and excessive sludge generation. .
본 발명은 상기와 같은 폐단을 해결하기 위해 생물막 여과 공정을 이용한 원수 전처리 및 고도 정수 장치를 개발하였다.The present invention has developed a raw water pretreatment and advanced water purification device using a biofilm filtration process to solve the above-mentioned waste.
이 방법은 암모니아 성질소 제거가 거의 100% THMs 발생은 전혀 일어나지 않으면서도 원수중의 DOC, COD, THMFP, BOD, SS, Color, E254, Chla, KMnO4소비량등 오염물질인 냄새 원인 물질을 동시에 제거하여 원수수질을 4∼5급수에서 1∼2급수로 개선할 수 있어 양질의 상수원수를 공급할 수 있는 장치를 발명한 것으로 그 실시예에 따라 상세히 설명하면 다음과 같다.This method simultaneously removes odor-causing substances such as contaminants such as DOC, COD, THMFP, BOD, SS, Color, E 254 , Chla, and KMnO 4 consumption in raw water, while eliminating ammonia. By removing the raw water quality can be improved from 4 to 5 grades to 1 to 2 grades, the invention is invented a device capable of supplying a good quality of raw water is described in detail according to the embodiment.
도1은 본 발명의 정수처리 공정도.1 is a water treatment process diagram of the present invention.
도2는 종전의 정수처리 공정도.2 is a conventional water purification process.
도3은 본 발명의 상수원수 전처리 장치도.Figure 3 is a water supply pretreatment apparatus of the present invention.
도4는 본발명의 고도 정수 장치도.4 is an elevation water purification apparatus of the present invention.
도5는 종전의 침전지를 이용한 생물막 여과 장치도.5 is a biofilm filtration device using a conventional sedimentation basin.
도6은 본 발명의 생물막 여과지의 상세도.Figure 6 is a detailed view of the biofilm filter paper of the present invention.
〈도면의 주요 부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>
1;침사지 2;약품혼화지 3;floc 형성조 4;생물막 여과 공정1; settled paper 2; chemical mixing paper 3; floc forming tank 4; biofilm filtration process
5;오존공정 6;생물활성탄(BAC)공정 a;유입관 b;배출관5; ozone process 6; bioactive carbon (BAC) process a; inlet pipe b; discharge pipe
c;공기주입관 d;역세정관c; air injection pipe d; backwashing pipe
실 시 예 1Example 1
원수 중에 토사나 SS를 침사지(1)에서 제거하고 약품혼화지(2)에서 혼합 믹싱하여 침전이 잘 되도록 물속의 미소 부유물질을 큰 입자로 바꾸는 floc 형성조(3)를 경유하고 생물막 여과 공정(4)을 통과시켜 배출관(b)으로 유출한다. 이때 생물막 여과지는 유입관(a)과 공기주입관(c)의 향류식으로 하고 용존산소가 높을 때는 공기 주입이 불필요하고 여재는 제오카본이나 BAC공정의 파과된 입상활성탄 섬유 Ball 여재를 충진하여 이용한다. 충진여재층이 폐색되는 경우 역세정관(d)으로 역세수를 공급한다.Biofilm filtration process through the floc forming tank (3) which removes the soil and SS from the raw water from the sedimentation basin (1) and mixes and mixes it in the chemical mixing paper (2) to convert the fine suspended solids in the water into large particles so that they are precipitated. 4) is passed through the discharge pipe (b). At this time, the biofilm filter paper is a counterflow type of the inflow pipe (a) and the air injection pipe (c). When the dissolved oxygen is high, air injection is unnecessary and the filter medium is filled with the broken carbon activated carbon fiber ball filter of the zeocarbon or BAC process. . If the filling medium layer is blocked, backwash water is supplied to the backwashing tube (d).
실 시 예 2Example 2
생물막 여과지를 부설할 여분의 부지가 없는 기존 정수장의 개선을 위해서는 침전지(1) 내에서 Honeycomb 또는 생물막 여과공정(4)을 부설하여 생물막 여과에 의해 전처리한 후 후속공정인 오존공정(5)과 생물활성탄(BAC)공정(6)을 통과시켜 정수한다.In order to improve the existing water purification plant where there is no extra site to install the biofilm filter paper, the Honeycomb or the biofilm filtration process (4) is laid in the sedimentation basin (1), pretreated by biofilm filtration, and then the ozone process (5) and the subsequent process Purified by passing through the activated carbon (BAC) step (6).
실 시 예 3Example 3
생물막여과공정(4)에 의한 원수 전처리 후 오존 공정(5)을 거쳐 잔자갈 또는 굵은 모래층에 의해 지지되는 생물활성탄(BAC) 공정(6)을 통과시켜 정수를 한다.After the raw water pretreatment by the biofilm filtration step (4), the ozone step (5) is passed through a bioactive carbon (BAC) step (6) supported by a residue or coarse sand layer to purify the water.
원수 수질 및 수온에 따라 생물막 여과 공정(4)을 통과한 물을 오존 공정(5)을 거치지 않고 By pass pipe를 통하여 생물활성탄(BAC) 공정(6)으로 보내어 정수처리를 한다.Depending on the raw water quality and the water temperature, the water passed through the biofilm filtration process (4) is sent to the bioactive carbon (BAC) process (6) through a by-pass pipe without undergoing the ozone process (5) for water purification.
이와 같은 실시예를 거쳐 정수되는 본 발명의 생물막 여과 공정(4)을 이용한 원수 전처리 장치는 여재표면에 부착한 미생물막은 유입 침사지(1) 원수 중의 부유물은 물론 용존 유기물이 약품혼화조(2)와 floc형성조(3)에서 floc을 형성하여 유입하는 원수를 산화분해 하기 때문에 오존공정(5)과 생물활성탄 BAC 공정(6)을 거치는 동안 정수되면서 여과 효과까지 얻을 수 있어 원수전처리에 매우 적합한 장치이다. 특히, 생물막 여과 공정(4)의 여과속도가 100∼120m/day이상(여재에 따라서는 수백m/day도 가능)으로서 급속여과지와 거의 같은 면적으로서 전처리 효과를 기대할 수 있어 매우 경제적인 방법임을 알 수 있다. 생물막 여과 공정(4)에 의한 원수 전처리 장치의 원수 수질의 처리효과는 NH4-N 95∼100%, BOD 70∼80%, COD 50%, DOC 50%이상, THMFP 50%, 탁도 95%이상, Color 70∼80%, SS 100%, Chl-a 90%이상, E25460%, KMnO4 소비량 50%의 제거율을 나타냈다.In the raw water pretreatment apparatus using the biofilm filtration process (4) of the present invention purified through the above-described embodiment, the microbial membrane attached to the surface of the media is the inflow settlement (1) and the suspended organic matter as well as the dissolved organic matter in the chemical mixing tank (2). Since the floc is formed in the floc forming tank (3) to oxidatively decompose the incoming water, it is very suitable for raw water pretreatment as it can be purified and filtered during the ozone process (5) and the bioactive carbon BAC process (6). . In particular, the filtration rate of the biofilm filtration process (4) is 100 to 120 m / day or more (hundreds of m / day depending on the filter medium), and the pretreatment effect can be expected to be about the same area as that of the rapid filter paper. Can be. The raw water quality treatment effect of the raw water pretreatment device by the biofilm filtration process (4) is NH 4 -N 95-100%, BOD 70-80%, COD 50%, DOC 50% or more, THMFP 50%, turbidity 95% or more The removal rate was 70-80%, SS 100%, Chl-a 90%, E 254 60%, and KMnO4 consumption 50%.
생물막 여과 공정(4) 이후에 연계되는 공정은 후 오존(post ozonation)공정(5)과 입상활성탄공정에 의하여 생물활성탄(BAC) 공정(6)으로 구성된다. 고탁도 및 수질악화시 생물막공정 전단부에 설치된 floc 성형조(3)의 응집공정에 의해 제거가능하며 약품혼화지(2)의 응집약품 주입정도에 따라 후 오존공정(5)을 생략할 수도 있다. 이 방법은 기존 급속여과 시스템을 생물막 여과에 의해 고도처리 시스템으로 개선할 때 이용하는 방법이다.The process linked after the biofilm filtration process (4) is composed of a bioactive carbon (BAC) process (6) by a post ozonation process (5) and granular activated carbon process. During high turbidity and water deterioration, the floc forming tank 3 installed at the front end of the biofilm process can be removed by the flocculation process, and the post ozone process 5 may be omitted depending on the degree of incorporation of the flocculant in the chemical admixture paper 2. . This method is used to upgrade existing rapid filtration systems to advanced treatment systems by biofilm filtration.
하기 표는 본 발명의 공정라인과 종전라인의 운전 조건 비교 표임.The following table is a comparison table of the operating conditions of the process line and the previous line of the present invention.
하기표는 본 발명의 공정과 종전 공정라인의 평균 유입 수질에 대한 실험 결과 비교 표임.The following table is a comparison of the experimental results for the average influent water quality of the process of the present invention and the previous process line.
하기표는 본 발명의 공정과 종전 공정 라인의 고탁도 유입 및 수질악화시의 실험 결과 비교 표임.The following table is a comparison of the experimental results during high turbidity inflow and water quality of the process of the present invention and the previous process line.
이와 같은 본 발명의 전처리 장치 및 고도 처리 장치는 시급한 상수원수의 수질 개선과 정수질개선에 큰 기여를 할 수 있음을 알 수 있으며 기존의 정수시설이 완비된 상태에서 생물막 여과 공정을 도입할 경우 침전지의 일부에 생물막 여과공정을 설치하면 침전지에 충분한 잔여 부지를 확보할 수 있고 정수장을 보다 유효하게 이용할 수가 있다.It can be seen that the pretreatment device and the advanced treatment device of the present invention can greatly contribute to water quality improvement and water purification improvement of urgent water source, and when the biofilm filtration process is introduced in the state of existing water purification facilities, the sedimentation basin The installation of a biofilm filtration process in part of the can ensure sufficient remaining land in the sedimentation basin and make the water treatment plant more effective.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20040034987A (en) * | 2002-10-18 | 2004-04-29 | 김관호 | The seawater filtration method for a red tide prevention |
KR100461493B1 (en) * | 2002-08-09 | 2004-12-10 | 현대모비스 주식회사 | Water processing apparatus unifying ozone reactor and filtration equipment and the method for water purification thereby |
KR100502957B1 (en) * | 2002-09-05 | 2005-07-21 | 금강엔지니어링 주식회사 | Reactor Comprising PBAC Carrier and Water Treatment Method Using the Same |
KR100853452B1 (en) * | 2007-06-27 | 2008-08-21 | (주)범한엔지니어링 종합건축사 사무소 | Apparatus for treatment bank filtered water including iron and manganese |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101023437B1 (en) * | 2005-01-20 | 2011-03-24 | 동아대학교 산학협력단 | Advanced Water Treatment System using Biofilm Filtration and Membrane Separation |
KR100716766B1 (en) | 2005-08-02 | 2007-05-14 | 이희권 | Waste Water Disposal Plant By Media Biofilter |
KR101903043B1 (en) | 2018-04-27 | 2018-10-01 | 주식회사 대성그린테크 | Advanced oxidation, adsoption system for control of micropollutants in wastewater |
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1999
- 1999-11-24 KR KR1019990053654A patent/KR100325830B1/en not_active IP Right Cessation
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100461493B1 (en) * | 2002-08-09 | 2004-12-10 | 현대모비스 주식회사 | Water processing apparatus unifying ozone reactor and filtration equipment and the method for water purification thereby |
KR100502957B1 (en) * | 2002-09-05 | 2005-07-21 | 금강엔지니어링 주식회사 | Reactor Comprising PBAC Carrier and Water Treatment Method Using the Same |
KR20040034987A (en) * | 2002-10-18 | 2004-04-29 | 김관호 | The seawater filtration method for a red tide prevention |
KR100853452B1 (en) * | 2007-06-27 | 2008-08-21 | (주)범한엔지니어링 종합건축사 사무소 | Apparatus for treatment bank filtered water including iron and manganese |
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