KR960009377B1 - Apparatus and method for waste water treatment by combined system with reverse osmosis and pelite - Google Patents
Apparatus and method for waste water treatment by combined system with reverse osmosis and pelite Download PDFInfo
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- KR960009377B1 KR960009377B1 KR1019930027691A KR930027691A KR960009377B1 KR 960009377 B1 KR960009377 B1 KR 960009377B1 KR 1019930027691 A KR1019930027691 A KR 1019930027691A KR 930027691 A KR930027691 A KR 930027691A KR 960009377 B1 KR960009377 B1 KR 960009377B1
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- reverse osmosis
- ferrite
- plating
- waste water
- 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
- 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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F1/48—Treatment of water, waste water, or sewage with magnetic or electric fields
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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
- C02F2103/16—Nature of the water, waste water, sewage or sludge to be treated from metallurgical processes, i.e. from the production, refining or treatment of metals, e.g. galvanic wastes
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- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
제1도는 본 발명의 방법을 수행하는 장치개념도.1 is a conceptual diagram of an apparatus for carrying out the method of the present invention.
제2도는 본 발명의 결과 시험그래프(아연제거율).2 is a test graph (zinc removal rate) of the results of the present invention.
제3도는 본 발명의 결과 시험그래프(아연페라이트회수율).3 is a test graph of the results of the present invention (zinc ferrite recovery).
본 발명은 역삼투압과 페라이트법의 혼성시스템에 의한 도금폐수처리방법과 장치에 관한 것으로 더 상세하게는 도금공정시 발생되는 도금폐수를 역삼투압법으로 처리하여 얻은 투과수는 도금수세수로 재사용하고, 농축된 중금속 이온은 페라이트법에 의해 페라이트분말로 회수하므로써 도금폐수가 밖으로 배출되지 않는 역삼투 및 페라이트법에 의한 혼성시스템인 무배출방법과 이를 수행하는 장치이다.The present invention relates to a plating wastewater treatment method and apparatus by a hybrid system of reverse osmosis and ferrite method, and more particularly, the permeated water obtained by treating the plating wastewater generated by the plating process with reverse osmosis is reused as the plating wash water. In addition, the concentrated heavy metal ions are a non-discharge method which is a hybrid system by reverse osmosis and ferrite method in which the plating wastewater is not discharged out by recovering the ferrite powder by the ferrite method and the apparatus for performing the same.
도금공업에서 도금후 발생하는 도금폐수는 현재 침전응집법에 의해 처리한후 중금속은 슬러지화 하고, 슬러지를 여과한 여액은 방류하고 있는 실정이다. 현 침전응집법은 설치비가 많이 들고 도금폐수중에서 중금속이온 뿐만 아니라 유해유기약품, 계면활성제 및 광택제 등이 들어있어 완전침전이 어렵고, 이를 처리하기 위하여 많은 화학약품을 사용한다. 위의 문제점외에도 침전응집법은 처리후 많은 약품의 사용에 의해 중금속이온의 약 100배에 달하는 화학적으로 불안정한 슬러지가 발생되어 이의 매립에 의한 중금속 재용해 등으로 토질 및 수질의 오염 가능성이 있다.The plating wastewater generated after plating in the plating industry is currently treated by sedimentation agglomeration, and heavy metals are sludged, and the filtrate after sludge is filtered is discharged. The current precipitation coagulation method is expensive to install and contains heavy organic ions, surfactants, and brighteners as well as heavy metal ions in the plating wastewater, making it difficult to completely settle and use many chemicals to treat them. In addition to the above problems, the precipitation flocculation method generates chemically unstable sludges of about 100 times the heavy metal ions due to the use of many chemicals after treatment, and there is a possibility of soil and water pollution due to heavy metal re-dissolution by landfill.
본 발명은 이와같은 종래의 결정을 해소코져 도금폐수가 밖으로 배출되지 않게 하기 위하여 세정 및 수세에서 발생하는 중금속이온농도가 적은 도금폐수를 역삼투압으로 처리하여 투과수는 재사용하고, 농축된 아연, 니켈 등의 중금속이온은 페라이트공정으로 보내져 페라이트분말로 회수하므로써, 환경적으로 오염이 없는 무배출공정이 가능한 것이다.In order to solve such a conventional crystal, the present invention treats the plating wastewater having a low concentration of heavy metal ions generated by washing and washing with reverse osmosis so that the plating wastewater is not discharged out. Heavy metal ions, such as these, are sent to the ferrite process and recovered as ferrite powder, thereby enabling an environment-free pollution-free process.
이하 발명의 요지를 공정장치인 제1도에 연계시켜 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to FIG. 1 as a process apparatus.
처리공정Process
도금폐수가 방출되면 모래여과장치(sand filter) 1과 정밀여과장치(micro filter) 2를 거쳐 고형물, 먼지 및 모래 등을 제거시킨다. 4는 한외여과장치(ultrafilter)로 1 및 2에 의해 제거되지 않는 유기물계통인 계면활성제, 킬레이트 화합물을 제거시킴으로 역삼투막에서 가장 큰 장애요인의 하나인 fouling을 제거시킨다. 세정조 3과 6에 있는 세정수는 한외여과막과 역삼투막에 각각 세정수를 역으로 흐르게 하여 막을 세정시키는 역할을 한다. 4의 한외과여과막장치에서 부과되어 나온 도금폐수는 저장탱크 5에 모아진 다음 용액의 pH를 조절한 후 역삼투압(reverse osmosis)장치 7로 간다. 여기서 도금폐수중 역삼투압막을 통과한 투과수는 도금용수로 재사용하고, 농축된 중금속이온은 페라이트반응장치 9로 보낸다. 페라이트반응조의 반응온도는 60-90℃ 정도로 하고 Fe(Ⅱ) 혹은 Fe(Ⅲ) 적당량과 NaOH와 같은 알카리를 당량만큼 첨가한 후 산소를 불어넣어 Fe(Ⅱ)를 산화시키면서 페라이트분말을 생성시킨다. 자력선별장치(Nagnetic separator) 10을 이용해서 페라이트분말을 분리해 내어 건조기 11에서 건조시킨다.When the plating wastewater is discharged, the solids, dust and sand are removed through a sand filter 1 and a micro filter 2. 4 is an ultrafilter to remove fouling, one of the biggest obstacles in reverse osmosis membranes, by removing surfactants and chelating compounds, which are organic compounds that are not removed by 1 and 2. The washing water in the washing tanks 3 and 6 serves to wash the membrane by flowing the washing water backward to the ultrafiltration membrane and the reverse osmosis membrane, respectively. Plating wastewater discharged from the ultrafiltration membrane apparatus of 4 is collected in the storage tank 5, and then the pH of the solution is adjusted to the reverse osmosis apparatus 7. Here, the permeated water that has passed through the reverse osmosis membrane in the plating wastewater is reused as plating water, and the concentrated heavy metal ions are sent to the ferrite reactor 9. The reaction temperature of the ferrite reactor is about 60-90 ° C, and an appropriate amount of Fe (II) or Fe (III) and alkali such as NaOH are added in an equivalent amount, and oxygen is blown to produce ferrite powder by oxidizing Fe (II). The ferrite powder is separated using a magnetic separator 10 and dried in a dryer 11.
실시예Example
아연농도가 58ppm, pH 2.2, 탁도가 10인 아연계도금실폐수를 정밀여과, 한외여과 및 역삼투 장치로 처리하여 얻은 투과수의 탁도를 측정한 결과 탁도는 각각 4.2, 1.5 및 0.5이었고, pH를 변화하여 역삼투장치로 처리한 결과 pH 8.0 이상에서 아연제거율은 99.9% 이상이었다.(제2도)The turbidity of the permeate obtained by treatment of zinc-plated wastewater with a zinc concentration of 58 ppm, pH 2.2, and turbidity of 10 with microfiltration, ultrafiltration, and reverse osmosis was measured, and the turbidities were 4.2, 1.5, and 0.5, respectively. As a result of treatment with reverse osmosis device, zinc removal rate was more than 99.9% at pH 8.0 or above.
역삼투장치에 의해 농축된 아연도금폐수 농축액에 제1철 이온을 첨가하고 산소를 불어넣어 반응시킨 결과 반응온도 80℃, pH9.0-10.0, Zn/Fe의 몰비 0.5-0.6 사이에서 아연페라이트를 얻었다.(제3도)Zinc ferrite was added at a reaction temperature of 80 ° C, pH9.0-10.0, and Zn / Fe molar ratio of 0.5-0.6. (Figure 3)
그러므로 본 발명은 현재 공해문제에 주요요인으로 되고 있는 도금산업 분야에 널리 실용화시켜 환경보호에 기여할 수 있는 것이다.Therefore, the present invention can contribute to environmental protection by making it widely practical in the field of plating industry, which is currently a major factor in the pollution problem.
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