KR20010045515A - Wastewater Disposal agent And Process For Preparing thereof - Google Patents
Wastewater Disposal agent And Process For Preparing thereof Download PDFInfo
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- KR20010045515A KR20010045515A KR1019990048828A KR19990048828A KR20010045515A KR 20010045515 A KR20010045515 A KR 20010045515A KR 1019990048828 A KR1019990048828 A KR 1019990048828A KR 19990048828 A KR19990048828 A KR 19990048828A KR 20010045515 A KR20010045515 A KR 20010045515A
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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
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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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
- C02F2103/06—Contaminated groundwater or leachate
Abstract
Description
본 발명은 폐수처리제 및 그 제조 방법에 관 한 것으로,특히 쓰레기 매립지에서 발생되는 침출수와, 염색공장 등의 산업현장에서 배출되는 폐수 중의 색도(Color)및 오염 물질 [COD,BOD,SS(부유물)]을 경제적으로 처리하는 폐수 처리제 및 그 제조방법에 관한 것이다.The present invention relates to a wastewater treatment agent and a method for manufacturing the same, in particular leachate generated from landfills and wastewater discharged from industrial sites such as dyeing factories (Color) and pollutants [COD, BOD, SS (float) ] To treat the wastewater economically and a method of manufacturing the same.
일반적으로 쓰레기 매립지에서 발생되는 침출수나, 염료공장 및 염색공장등에서 배출되는 염색 폐수에 사람은 물론 자연환경을 오염 시키는 유해 물질 즉, 색도 및 부유물질(SS)이 많이 함유되어 있음은 물론 화학적 산소요구량(COD),생물학적 산소요구량(BOD)이 상당히 높은 악성 폐수임은 주지된 사실이다.In general, leachate from waste landfill or dye wastewater discharged from dye factories and dyeing factories contains not only humans but also harmful substances that contaminate the natural environment such as color and suspended solids (SS) as well as chemical oxygen demand. It is well known that COD and BOD are significantly higher malignant wastewater.
종래 이러한 유해한 오염 물질의 처리 방법을 보면 다음과 같은 방법들을 이용하고 있다. 첫째는 국내 등록특허공고 등록번호 제145467호(98.4.30)'염색폐수 처리방법과 그 장치'에 개시된 바와 같은 생물학적 처리 공정을 거친후 화학적 처리공정으로 처리하는 방법과, 둘째는 화학적 처리공정을 거친후 생물학적으로 처리하는 방법과 그리고 때로는 상기 첫번째와 두번째 방법을 복합하여 2번 처리하는 경우가 있다. 이와 같은 여러 가지의 방법들에 있어서 화학적 처리 공정에서는 각종의 화학약품을 이용하여 폐수를 처리하고 있다.Conventionally, the method of treating such harmful pollutants uses the following methods. The first is a method of treating with a chemical treatment process after the biological treatment process as disclosed in Korean Patent Application Publication No. 145467 (98.4.30) 'Method and apparatus for dyeing wastewater,' and the second is a chemical treatment process. There is a case where the treatment with a biological treatment after coarse treatment and sometimes a combination of the first and second methods is performed twice. In these various methods, the chemical treatment process treats wastewater using various chemicals.
이와같은 화학적 처리 방법에 사용된 화학 약품에 의하면 산(Acid) 혹은 알칼리류 등과 같은 중화제, 염화 제1철 및 황산 제1철과 같은 무기응집제, 과산화수소수(H₂O₂)용액과 유기 고분자응집제 등을 사용하고 있다.Chemicals used in such chemical treatment methods include neutralizing agents such as acids or alkalis, inorganic coagulants such as ferrous chloride and ferrous sulfate, H 2 O 2 solution and organic polymer coagulants. Doing.
그러나 이러한 방법(일명 FENTON방법)에서는 전체 사용되는 화학 약품 중에서 가격이 고가인 과산화수소수가 차지하는 사용량이 많아서 그 만큼 폐수 처리에 소요되는 비용을 높아지게 하는 요인과, 또 고형물(Sludge)의 발생이 필요 이상으로 과다하게 되어 슬럿지의 처리비용을 많게하는 등의 비 효율성 및 비 경제적인 점이 있고, 또한 폐수처리의 효율도 대략 40 ~ 60% 정도에 불과 하다고 하는 문제도 있다.However, in this method (also known as the FENTON method), the use of hydrogen peroxide water, which is expensive, accounts for a large amount of the chemicals used, and thus increases the cost of wastewater treatment and the occurrence of sludge more than necessary. In addition, there is a problem that the efficiency of the waste water treatment is only about 40 to 60%, and there are also inefficiencies such as excessively increased sludge treatment costs.
한편 이러한 문제를 해소하기 위한 벙법으로 개발된 것들이 국내 등록특허 제148845호(1998.6.1등록)"신규한 폐수처리제 및 그 처리방법"과, 등록 제153331 호(1998.7.3)"폐수처리용 탈색 및 응결제 조성"과, 등록제 165526호(1998.9.16)"페수처리제의 제조방법"과, 공고번호 제85-1393호(1985.9.30)"용수 및 폐수처리용 응집제 조성물"등이 있으나,제조공정 등이 복잡하여 경제성이 떨어지는 단점이 있다.On the other hand, those developed as a method to solve this problem are registered in Korea Patent No. 148845 (registered on June 1, 1998) "New wastewater treatment agent and its treatment method" and Registration No. 153331 (1998.7.3) "Bleaching for wastewater treatment. And a coagulant composition ", Registration No. 165526 (1998.9.16)" Manufacturing method of wastewater treatment agent ", and Publication No. 85-1393 (1985.9.30)" Coagulant composition for water and wastewater treatment ", etc. There is a disadvantage that the economy is poor because the back is complicated.
따라서 본 발명의 목적은 상기 제반 결점들을 해소하고, 폐수중의 오염물질( 색도, 부유물질, BOD,COD)를 경제적이고 효율적으로 처리하기 위한 폐수 처리제 및 그 제조방법을 제공하는데에 있다.Accordingly, an object of the present invention is to provide a wastewater treatment agent and a method of manufacturing the same for eliminating the above-mentioned shortcomings, and for economically and efficiently treating pollutants (color, suspended matter, BOD, COD) in wastewater.
상기 목적을 달성하기 위해 본 발명의 폐수 처리제는 청구항1의 발명과 관련된 폐수중의 오염 물질을 처리하기 위한 처리제에 있어서, 황산 1 ~ 98중량(%)와, 황산 제1철(FeSO4,XH2O) 또는 염화 제1철(Fe Cl2,XH2O) 및 이들의 제1철 혼합물 중에서 선택한 어느하나의 약품 1 ~ 49중량(%)와, 황산 제2철[Fe₂(SO4)3] 또는 염화제2철(FeCl3,XH2O) 또는 이들의 제2철 혼합물중에서 선택된 어느 하나의 약품 1 ~ 50중량(%)를 혼합 교반하는 것을 특징으로 한다.In order to achieve the above object, the wastewater treatment agent of the present invention is a treatment agent for treating contaminants in wastewater related to the invention of claim 1, wherein 1 to 98% by weight of sulfuric acid and ferrous sulfate (FeSO 4, XH 2 O) or ferrous chloride (FeCl 2, XH 2 O) and any one selected from the ferrous mixture of 1 to 49% by weight of the drug, ferric sulfate [Fe₂ (SO 4 ) 3 Or ferric chloride (FeCl 3, XH 2 O) or a ferric compound selected from the mixture of ferric 1 to 50% by weight (%) is characterized by mixing and stirring.
상기 폐수 처리제의 총 중량에 대하여 이산화 티타늄 또는 티타늄 화합물중의 어느 하나의 약품을 0.01 ~ 999.9중량(%)를 더 포함함을 특징으로 한다.Regarding the total weight of the wastewater treatment agent, it is characterized in that it further comprises 0.01 to 999.9% by weight of the drug of any one of titanium dioxide or titanium compound.
또한 상기 목적을 달성하기 위해 본 발명의 폐수 처리제의 제조 방법은 청구항3의 발명과 관련된 폐수중의 오염 물질을 처리하기 위한 처리제의 제조방법에 있어서, 처리제는 황산 1 ~ 98중량(%)와, 황산 제1철(FeSO4,XH2O) 또는 염화 제1철(Fe Cl2,XH2O) 및 이들의 제1철 혼합물 중에서 선택한 어느하나의 약품 1 ~ 49중량(%)와, 황산 제2철[Fe₂(SO4)3] 또는 염화제2철(FeCl3,XH2O) 또는 이들의 제2철 혼합물중에서 선택된 어느 하나의 약품 1 ~ 50중량(%)를 탱크내에서 순차적으로 투입후 상온에서 혼합 교반하여 얻는 것을 특징으로 한다.In addition, the method for producing a wastewater treatment agent of the present invention in order to achieve the above object is a method for producing a treatment agent for treating contaminants in the wastewater according to the invention of claim 3, the treatment agent is 1 to 98% by weight (%) sulfuric acid, 1 to 49% by weight of any one selected from ferrous sulfate (FeSO 4, XH 2 O) or ferrous chloride (Fe Cl 2, XH 2 O) and ferrous mixtures thereof, and 1 to 50% by weight of one of the chemicals selected from ferric iron [Fe₂ (SO 4 ) 3 ] or ferric chloride (FeCl 3, XH 2 O) or ferric mixtures thereof is sequentially added into the tank. After the mixture is obtained by stirring at room temperature.
상기에서 무기 응집제인 황산제1철 및 염화제1철과, 황산 제2철및 염화제2철과, 이산화 티타늄 및 티타늄 화합물 등을 사용하여 만든 처리제(상품명; HI SOL)는 폐수중의 오염 물질을 산화 분해 시키는 화학 작용을 실행 하므로써, 추후 산화제로 투입하게 되는 과산화수소수의 소비량을 적게 한다.The treatment agent (trade name: HI SOL) made of ferrous sulfate and ferrous chloride, ferrous sulfate and ferric chloride, titanium dioxide and titanium compounds, etc., as the inorganic flocculant, are pollutants in wastewater. By carrying out the chemical action of oxidative decomposition, the consumption of hydrogen peroxide which is added to the oxidant later is reduced.
상기에서 이산화 티타늄 또는 티타늄 화합물의 투입 이유는 오염물질의 산화반응을 보다 활발하게 하기 위함이다.The reason for adding titanium dioxide or a titanium compound in the above is to more actively oxidize the pollutants.
이하, 본 발명에 따른 폐수 처리제 및 그 제조방법의 보다 바람직한 실시예를 상세히 설명한다.Hereinafter, a more preferred embodiment of the wastewater treatment agent and its preparation method according to the present invention will be described in detail.
쓰레기 매립지에서 배출되는 침출수 및 염색공장 등에서 배출되는 염색 폐수는 원수조의 내부로 유입되어 저류되며, 이때 폐수에 함유된 오염물질은 대체적으로 물리적 처리단계, 화학적 처리단계 및 고액분리 단계를 통하여 처리되는데, 본원 발명은 상기 화학적 처리 단계에서 과산화수소수와 같이 화학적 처리제로 사용되는 것이다.Leachate discharged from landfills and dyeing wastewater discharged from dyeing factories are stored in the raw water tank and stored.In this case, pollutants contained in the wastewater are treated through physical treatment, chemical treatment and solid-liquid separation. The present invention is to be used as a chemical treatment agent such as hydrogen peroxide in the chemical treatment step.
〈실시예1〉<Example 1>
황산 98중량(%)와, 황산 제1철(FeSO4,XH2O) 또는 염화 제1철(FeCl2,XH2O) 또는 이들의 혼합물 중에서 선택한 어느하나의 약품 1중량(%)와, 황산 제2 철 [Fe₂(SO4)3] 또는 염화제2철(FeCl3,XH2O) 또는 이들의 혼합물중에서 선택된 어느 하나의 약품 1중량(%)와를 탱크내에 순차적으로 투입후 상온에서 혼합 교반하여 폐수중의 오염 물질을 처리하기 위한 처리제(상품명 HISOL)를 수득하였다.98 wt% sulfuric acid , 1 wt% chemical of any one selected from ferrous sulfate (FeSO 4, XH 2 O) or ferrous chloride (FeCl 2, XH 2 O), or a mixture thereof, 1 weight (%) of any one of chemicals selected from ferric sulfate [Fe₂ (SO 4 ) 3 ] or ferric chloride (FeCl 3, XH 2 O) or a mixture thereof is sequentially added into a tank and mixed at room temperature. Stirring gave a treating agent (trade name HISOL) for treating contaminants in wastewater.
이렇게 얻은 처리제와 종래의 처리제 약품(FeCl₂)을 침출수 및 염색공장에서 배출되는 원폐수 1톤에 대하여 표 1의 표시와 같은 양을 투입후 이어서 투입되는 과산화수소수의 투입량과 최종 발생되는 슬럿지(고형물)와 COD의 감소량을 비교 측정하였다. 그 결과는 표1과 같았다.The amount of hydrogen peroxide water added and the final sludge produced (solids) were added to the treatment agent and the conventional treatment agent (FeCl₂) in the amount shown in Table 1 for 1 ton of wastewater discharged from leachate and dyeing plant. And reduction of COD were measured. The results are shown in Table 1.
〈실시예2〉<Example 2>
상기 실시예1로 부터 얻은 폐수 처리제 총 중량에 대해 이산화 티타늄 또는 티타늄 화합물중의 어느 하나의 약품을 0.01 ~ 999.9중량(%)를 첨가하여 폐수중의 오염 물질을 처리하기 위한 처리제(상품명 HISOL)를 수득하였으며, 이렇게 얻은 처리제를 원 폐수 1톤에 대하여 표1의 표시와 같은 같은 양을 투입한후 이어서 투입되는 과산화수소수의 투입량과 최종 발생되는 슬럿지(고형물)와 COD의 감소량을 비교 측정하였다. 그 결과는 표1의 표시와 같았다.A treatment agent (trade name HISOL) for treating contaminants in wastewater was added by adding 0.01 to 999.9% by weight of any one of titanium dioxide or a titanium compound to the total weight of the wastewater treatment agent obtained from Example 1. The treatment agent thus obtained was subjected to the same amount as shown in Table 1 with respect to 1 ton of raw wastewater, and then the amount of hydrogen peroxide solution introduced, the amount of sludge produced (solid) and the amount of reduction in COD were compared. The results were as shown in Table 1.
상기 표1로부터 확인되는바와 같이, 폐수의 오염물질의 처리에 있어서 본 발명의 처리제를 사용하는 경우 종래에 약품 투입에 비해 고가로 되는 과산화수소수의 사용량이 현저하게 감소됨을 알수가 있고, 또한 종래에 비하여 슬럿지의 발생율과 COD가 현저하게 감소되는 사실을 알수가 있다.As can be seen from Table 1, when the treatment agent of the present invention is used in the treatment of contaminants in wastewater, it can be seen that the amount of hydrogen peroxide water, which is expensive compared to the conventional chemical input, is significantly reduced. In comparison, the incidence of sludge and COD are significantly reduced.
또 상기 실시 예들로부터 만들어진 처리제는 보관시 침전물이 발생되는 것을 억제 하기위해 교반기나 혹은 에어 교반을 갖추어 놓는 것이 바람 직하다.In addition, the treatment agent made from the above embodiments is preferably equipped with a stirrer or air agitation in order to suppress the generation of deposits during storage.
또한 상기 실시 예에서는 설명하지 않았으나 수 처리제 있어서 알루미늄용액을 산 보조제로 사용하면 폐수를 효과적으로 처리할수도 있다.In addition, although not described in the above embodiment, when the aluminum solution is used as an acid aid in the water treatment agent, the wastewater may be effectively treated.
이상과 같이 본 발명에 의하면, 폐수의 오염물질을 화학적으로 처리하는 데에 사용하는 처리제를 황산제1철 및 염화제1철과 아울러 황산 제2철및 염화제2철 등의 철용액과, 티타늄 화합물 등의 산화제를 혼합 교반하여 된 것에 의해, 차후 과산화수소수의 투입량을 감소 시킬수 있는 효과와, 또 슬러지의 발생량을 적게하여 슬럿지의 처리시 처리 비용을 줄일수 있는 효과가 있고, 또한 종래의 투입되는 약품량에 비하여 적게 투입을 하더라도 폐수중의 오염물질 즉, BOD,COD 등을 현저하게 줄일 수 있는 효과가 있다.As described above, according to the present invention, a treatment agent used for chemically treating contaminants in wastewater is ferrous sulfate and ferric chloride, iron solution such as ferric sulfate and ferric chloride, and titanium. By mixing and stirring the oxidizing agent such as a compound, it is possible to reduce the input amount of hydrogen peroxide in the future, and to reduce the generation cost of the sludge by reducing the amount of sludge generated, and also to add the conventional input Even if the amount is less than the amount of chemicals, there is an effect that can significantly reduce the contaminants in the waste water, that is, BOD, COD.
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