KR100193785B1 - Wastewater Treatment and Reuse Method using Microfiltration and Reverse Osmosis Membrane and Its Apparatus - Google Patents

Wastewater Treatment and Reuse Method using Microfiltration and Reverse Osmosis Membrane and Its Apparatus Download PDF

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KR100193785B1
KR100193785B1 KR1019970015551A KR19970015551A KR100193785B1 KR 100193785 B1 KR100193785 B1 KR 100193785B1 KR 1019970015551 A KR1019970015551 A KR 1019970015551A KR 19970015551 A KR19970015551 A KR 19970015551A KR 100193785 B1 KR100193785 B1 KR 100193785B1
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hydrofluoric acid
treated water
solids
acid wastewater
reverse osmosis
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KR19980078119A (en
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이태준
황재동
이진영
이원권
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양인모
삼성엔지니어링주식회사
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Abstract

본 발명은 불산을 포함하는 폐수 처리 및 재이용 방법과 그 장치에 관한 것으로서, 본 발명에서는 정밀여과 및 역삼투막을 이용하여 산업 현장에서 발생하는 불산 폐수를 처리하여, 별도의 여과 단계를 거치지 않고서도 배출수를 공업 용수로 재생 이용할 수 있도록 한다. 본 발명에 의한 불산 폐수 처리 방법은 응집제를 사용하여 pH를 조정함과 동시에 산폐수에 포함된 불소 이온을 고형화된 불소화합물화하고 응집보조제에 의하여 형성된 고형물을 조대화하는 단계; 상기 단계에서 조대화된 고형물을 정밀여과에 의하여 분리하여 탁도성분을 포함하는 고형물과 고형물이 제거된 처리수를 배출하는 단계; 상기 단계에서 배출된 처리수에 포함된 유기물을 활성탄을 이용하여 흡착하여 제거하는 단계; 및 상기 단계에서 유기물이 제거된 처리수에 포함된 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재이용 가능한 처리수를 배출하는 단계를 포함하는 것을 특징으로 한다.The present invention relates to a wastewater treatment and reuse method and apparatus therefor including hydrofluoric acid, and in the present invention, by treating hydrofluoric acid wastewater generated in an industrial site using microfiltration and reverse osmosis membrane, the wastewater is discharged without undergoing a separate filtration step. Recyclable industrial water. Hydrofluoric acid wastewater treatment method according to the present invention comprises the steps of adjusting the pH using a flocculant and at the same time solidifying fluorine fluoride ions contained in the acid wastewater and coarsening the solids formed by the flocculating aid; Separating the coarse solids in the step by microfiltration to discharge the solids containing the turbidity component and the treated water from which the solids are removed; Adsorbing and removing the organic matter contained in the treated water discharged in the step using activated carbon; And removing unreacted fluorine ions, other dissolved salts, and residual organic matters contained in the treated water from which the organic matter was removed using a reverse osmosis membrane to discharge the reusable treated water.

Description

정밀여과와 역삼투막을 이용한 불산 폐수 처리 및 재이용 방법과 그 장치Wastewater Treatment and Reuse Method using Microfiltration and Reverse Osmosis Membrane and Its Apparatus

본 발명은 불산 폐수의 처리 및 재이용 방법과 그 장치에 관한 것이다.The present invention relates to a method and apparatus for treating and recycling hydrofluoric acid wastewater.

불산에 포함된 불소 이온은 독성이 있는 것으로 밝혀져서, 물 속에 3㎎/ℓ이상 포함되어 있으면 수중 생태계에 영향을 미치고, 인체에 들어가면 위와 장, 순환계 및 신경계에 이상을 나타내면 각종 질병을 일으킬 수 있다고 보고되어 있다.Fluoride ions contained in hydrofluoric acid have been found to be toxic, and containing more than 3mg / l in water affects the aquatic ecosystem, and if it enters the human body, it can cause various diseases if abnormal in stomach, intestines, circulatory system and nervous system. Reported.

불산은 전자 및 항공산업에서 표면처리, 세정 및 식각 공정에서 사용되고, 이러한 불산 폐수의 종래 처리 방법은 응집, 침전, 여과 또는 흡착에 의하여 용존 불산을 고형화하여 침전시킨 후, 방류하거나 불소 이온을 선택적으로 흡착하는 흡착제를 이용하여 흡착 후 방류하고 있다.Hydrofluoric acid is used in the surface treatment, cleaning and etching processes in the electronics and aviation industries. Such conventional treatment of hydrofluoric acid wastewater solidifies and precipitates dissolved hydrofluoric acid by flocculation, precipitation, filtration or adsorption, and then discharges or selectively fluorine ions. It discharges after adsorption using the adsorption agent which adsorb | sucks.

응집, 침전법에 의한 처리 방법은 슬러지 발생이 많고, 넓은 시설 면적을 필요로 하며 현재의 법정 방류수 수질 기준을 만족시키기는 하나 처리수의 불소 농도가 높아서 중·소 하천에 많은 량의 폐수가 방류될 때 오염부하율이 증대되어 농작물 및 어류에 피해를 입힐 수 있다.The treatment method by flocculation and sedimentation method generates a lot of sludge, requires a large facility area, and satisfies the current legal effluent water quality standards, but has a high concentration of fluorine in the treated water, so a large amount of wastewater is discharged into small and medium streams. Can increase the load of pollutants and damage crops and fish.

흡착제를 이용하여 흡착 후 방류하는 방법은 처리수의 불소 농도를 감소시킬 수는 있으나 흡착을 위한 별도의 설비가 필요하고 주기적으로 재생을 위한 많은 화학약품을 필요로 할 뿐만 아니라, 알루미늄 이온과 같은 방해 물질이 있는 경우 흡착 용량이 저하되는 단점이 있다. 또한, 흡착제를 이용하는 방법은 폐수 중 불소 이온의 농도가 높은 경우 장치가 거대해지고 재생빈도가 높으며, 재생 폐수를 처리하기 위한 별도의 시설을 필요로 한다.The discharge method after adsorption using an adsorbent can reduce the fluorine concentration in the treated water, but requires a separate facility for adsorption and requires many chemicals for periodic regeneration, as well as interference such as aluminum ions. If there is a material has a disadvantage that the adsorption capacity is lowered. In addition, the method using the adsorbent has a large apparatus and a high regeneration frequency when the concentration of fluorine ions in the waste water is high, and requires a separate facility for treating the regeneration waste water.

또한, 종래의 불산 폐수 처리 방법은 불산 폐수 처리에 사용된 칼슘염에 의하여 처리수에 다량의 칼슘 이온이 존재하여 중수로 재이용시 관부식등을 유발하며 그밖에 무기염, 유기물, 탁도성분 등이 제거되지 않아서 공정수로 재이용이 불가능하다.In addition, the conventional hydrofluoric acid wastewater treatment method has a large amount of calcium ions in the treated water due to the calcium salt used in the hydrofluoric acid wastewater treatment, causing pipe corrosion when reused in heavy water, and other inorganic salts, organic matter, and turbidity components are not removed. Therefore, it cannot be reused as process water.

본 발명의 목적은 상기한 종래 방법들의 단점을 제거하기 위한 것으로서, 처리 효율이 높고, 약품 사용을 절감시켜서 슬러지 발생량을 감소시키며 비교적 간단한 설비를 사용하여 공업 용수로서 재이용이 가능한 처리수를 생산할 수 있는 불산폐수 처리 및 재이용 방법과 그 장치를 제공하는데 있다.An object of the present invention is to eliminate the drawbacks of the above-described conventional methods, the treatment efficiency is high, can reduce the use of chemicals to reduce the amount of sludge generated and can produce treated water that can be reused as industrial water using a relatively simple equipment To provide a method and apparatus for treating and recycling hydrofluoric acid wastewater.

도1은 본 발명의 바람직한 일실시예에 의한 불산폐수 처리 및 재이용 방법을 설명하는 공정도이다.1 is a flowchart illustrating a hydrofluoric acid wastewater treatment and reuse method according to an embodiment of the present invention.

* 도면의 주요한 부분에 대한 부호의 설명 *Explanation of symbols on the main parts of the drawings

10 : 저수조20 : 제1응집반응조10: reservoir 20: first flocculation reactor

30 : 제1정밀여과기40 : 활성탄흡착기30: first precision filter 40: activated carbon adsorber

50 : 역삼투기60 : 제2응집반응조50: reverse osmosis 60: the second flocculation reactor

70 : 제2정밀여과기70: second precision filter

상기한 목적을 달성하기 위한 본 발명에 의한 불산 폐수 처리 방법은, 응집제와 응집보조제를 사용하여 불산 폐수의 pH를 조정하고, 불산 폐수에 포함된 불소 이온을 고형화된 불소화합물화하고 형성된 고형물을 조대화하는 단계; 상기 단계에서 조대화된 고형물을 정밀여과에 의하여 분리하여 탁도성분을 포함하는 고형물과 고형물이 제거된 처리수를 배출하는 단계; 상기 단계에서 배출된 처리수에 포함된 유기물을 활성탄을 이용하여 흡착하여 제거하는 단계; 및 상기 단계에서 유기물이 제거된 처리수에 포함된 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재이용 가능한 처리수를 배출하는 단계를 포함하는 것임을 특징으로 한다.In the hydrofluoric acid wastewater treatment method according to the present invention for achieving the above object, the pH of the hydrofluoric acid wastewater is adjusted by using a flocculant and a coagulant adjuvant, and the fluorine ions contained in the hydrofluoric acid wastewater are solidified to form fluorine compounds. Talking; Separating the coarse solids in the step by microfiltration to discharge the solids containing the turbidity component and the treated water from which the solids are removed; Adsorbing and removing the organic matter contained in the treated water discharged in the step using activated carbon; And removing the unreacted fluorine ions, other dissolved salts, and residual organic matters contained in the treated water from which the organic matter was removed using a reverse osmosis membrane to discharge the reusable treated water.

상기한 본 발명에 의한 불산 폐수 처리 및 재이용 방법에서 불산 폐수의 pH를 조정하는 단계는 불산 폐수의 pH가 5.0 내지 7.5가 되도록 조정하는 것임을 특징으로 한다.In the hydrofluoric acid wastewater treatment and reuse method according to the present invention, the step of adjusting the pH of hydrofluoric acid wastewater is characterized in that the pH of the hydrofluoric acid wastewater is adjusted to 5.0 to 7.5.

또한, 상기한 목적을 달성하기 위한 본 발명에 의한 불산 폐수 처리 및 재이용 장치는, 응집제를 사용하여 불산 폐수의 pH를 조정하여, 산폐수에 포함된 불소 이온을 고형화된 불소화합물화하고 응집보조제에 의하여 형성된 고형물을 조대화하는 응집반응조; 상기 응집반응조에 의하여 조대화된 고형물을 정밀여과에 의하여 분리하여 탁도성분을 포함하는 고형물과 고형물이 제거된 처리수를 배출하는 정밀여과기; 상기 정밀여과기에 의하여 배출되는 처리수에 포함된 유기물을 활성탄을 이용하여 흡착하여 제거하는 활성탄흡착기; 및 상기 활성탄흡착기에 의하여 유기물이 제거된 처리수에 포함된 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재이용 가능한 처리수를 배출하는 역삼투기를 포함하는 것임을 특징으로 한다.In addition, the hydrofluoric acid wastewater treatment and reuse apparatus according to the present invention for achieving the above object, by adjusting the pH of the hydrofluoric acid wastewater using a flocculant, to solidify the fluorine ions contained in the acid wastewater and to the flocculation aid An agglomeration reaction tank for coarsening the solids formed by the same; A fine filter for separating the solid coarse by the coagulation reaction tank by fine filtration to discharge the solids containing the turbidity component and the treated water from which the solids are removed; Activated carbon adsorber for removing the organic matter contained in the treated water discharged by the precision filter by using the activated carbon; And a reverse osmosis unit which removes unreacted fluorine ions, other dissolved salts, and residual organic substances contained in the treated water from which the organic matter is removed by the activated carbon adsorber using a reverse osmosis membrane to discharge the treated water for reuse.

이하에서 첨부된 도면을 참조하면서 본 발명의 바람직한 일실시예를 상세하게 설명한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.

도1은 본 발명의 바람직한 일실시예에 의한 불산 처리 및 재이용 방법을 설명하는 공정도이다.1 is a flowchart illustrating a hydrofluoric acid treatment and reuse method according to an embodiment of the present invention.

불산 폐수가 저수조(10)에서 수집되어 저장된다. 저수조(10)에 저장된 불산 폐수는 제1응집반응조(20)에서, 응집제에 의하여 pH가 조정되고, 탁도 성분과 콜로이드 성분이 조대화되고 불소 이온은 고형화된 불소화합물로 전환된다. 사용되는 응집제로서 바람직한 것은 소석회, 탄산칼슘 및 폴리알루미늄클로라이드 등이다. 응집제에 의하여 pH가 5.0 내지 7.5가 되도록 조정된다. 또한, 고분자 응집 보조제에 의하여 고형화된 불소화합물과 탁도성분 및 고형유기물을 조대화시킬 수 있다.The hydrofluoric acid wastewater is collected and stored in the reservoir 10. The hydrofluoric acid wastewater stored in the storage tank 10 is pH-adjusted by the flocculating agent in the first aggregation reaction tank 20, the turbidity component and the colloidal component are coarsened, and the fluorine ions are converted into a solidified fluorine compound. Preferred flocculants used are hydrated lime, calcium carbonate, polyaluminum chloride and the like. The pH is adjusted to 5.0 to 7.5 by the flocculant. In addition, the fluorine compound, the turbidity component, and the solid organic matter solidified by the polymer coagulant may be coarsened.

제1응집반응조(20)에서 배출되는 불산폐수는 0.1 내지 0.2㎛의 기공을 가지는 관형 제1정밀여과기(30)로 유입되고, 제1정밀여과기(30)에 의하여 고형물이 분리되고 분리된 고형물은 제2응집반응조(60)로 배출되고, 고형물이 제거된 처리수는 활성탄흡착기(40)로 유입된다.The hydrofluoric acid wastewater discharged from the first flocculation reactor 20 is introduced into the tubular first precision filter 30 having pores of 0.1 to 0.2 μm, and the solids are separated and separated by the first precision filter 30. The treated water discharged to the second agglomeration reactor 60 and the solids are removed is introduced into the activated carbon adsorber 40.

활성탄흡착기(40)에서는 상기 제1정밀여과기(30)로부터 유입되는 처리수에 포함된 유기물을 활성탄을 이용하여 흡착 제거한다. 만약 불산 폐수에 유기물이 포함되어 있지 않는다면 활성탄흡착기(40)에 의한 처리 과정은 생략될 수 있다.The activated carbon adsorber 40 adsorbs and removes organic substances contained in the treated water flowing from the first precision filter 30 using activated carbon. If the organic acid is not included in the hydrofluoric acid wastewater, the treatment by the activated carbon adsorber 40 may be omitted.

역삼투기(50)는 상기 활성탄흡착기(40)로부터 배출되는 처리수에 포함되어 있는 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재생수를 배출하고, 역삼투막에 의하여 배제되어 농축된 용존 유기물 및 염을 포함하는 농축수는 제2응집반응조(60)로 배출된다.The reverse osmosis unit 50 removes unreacted fluorine ions, other dissolved salts, and residual organic substances contained in the treated water discharged from the activated carbon adsorber 40 using a reverse osmosis membrane to discharge the regenerated water, and is excluded by the reverse osmosis membrane and concentrated. The concentrated water containing the dissolved organic matter and salt is discharged to the second agglomeration reactor (60).

제2응집반응조(60)는 제1정밀여과기(30)로부터 유입되는 고형물과 역삼투기(50)로부터 유입되는 농축수 등을, 소석회 또는 탄산칼슘 및 폴리알루미늄클로라이드를 사용하여 고형화하고 흡착한 다음 고분자 응집 보조제에 의하여 조대화하여 제2정밀여과기(70)로 배출한다.The second agglomeration reactor 60 solidifies and adsorbs the solids introduced from the first precision filter 30 and the concentrated water introduced from the reverse osmosis unit 50 using hydrated lime or calcium carbonate and polyaluminum chloride, and then polymers. The coagulation agent is coarsened and discharged to the second fine filter 70.

제2정밀여과기(70)에서는 상기 제2응집반응조(60)로부터 유입되는 고형물들이 포함된 폐수를 여과 탈수하여 여액을 방류하고, 탈수된 고형물은 폐기물로서 배출한다.In the second precision filter 70, the wastewater containing the solids flowing from the second agglomeration reactor 60 is filtered and dewatered to discharge the filtrate, and the dehydrated solids are discharged as waste.

이상에서 설명한 바와 같은 본 발명에 의한 불산 폐수 처리 및 재이용 방법 과 그 장치에 의하여 배출되는 재생수는 일반적으로 사용되는 공업 용수보다 탁도가 우수하고 용존염 농도는 비슷한 수준을 유지하므로, 별도의 여과 단계를 거치지 않고 공업용수로서 재사용이 가능하다. 따라서, 별도의 여과 장치에 따른 초기 투자비 및 운전비가 들지 않고 용수를 공급할 수 있는 장점이 있다. 또한, 처리수가 재생이용될 수 있으므로 배출되는 폐수량과 공업 용수 사용량을 절감할 수 있다.As described above, the hydrofluoric acid wastewater treatment and reuse method according to the present invention and the regenerated water discharged by the apparatus have better turbidity and maintain dissolved salt concentrations similar to those of industrial water. It can be reused as industrial water without going through. Therefore, there is an advantage that the water can be supplied without the initial investment and operating costs according to a separate filtering device. In addition, the treated water can be recycled and can reduce the amount of waste water discharged and the amount of industrial water used.

Claims (3)

불산 폐수 처리 및 재이용 방법에 있어서,In the hydrofluoric acid wastewater treatment and reuse method, 응집제를 사용하여 불산 폐수의 pH를 조정하여 불산폐수에 포함된 불소 이온을 고형화된 불소화합물화하고 응집보조제에 의하여 형성된 고형물을 조대화하는 단계;Adjusting the pH of the hydrofluoric acid wastewater using a flocculant to solidify the fluorine ions contained in the hydrofluoric acid wastewater and to coarsen the solids formed by the flocculating aid; 상기 단계에서 조대화된 고형물을 정밀여과에 의하여 분리하여 탁도성분을 포함하는 고형물과 고형물이 제거된 처리수를 배출하는 단계;Separating the coarse solids in the step by microfiltration to discharge the solids containing the turbidity component and the treated water from which the solids are removed; 상기 단계에서 배출된 처리수에 포함된 유기물을 활성탄을 이용하여 흡착하여 제거하는 단계; 및Adsorbing and removing the organic matter contained in the treated water discharged in the step using activated carbon; And 상기 단계에서 유기물이 제거된 처리수에 포함된 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재이용 가능한 처리수를 배출하는 단계를 포함하는 것임을 특징으로 하는 불산 폐수 처리 및 재이용 방법.Treatment and reuse of hydrofluoric acid wastewater, characterized in that it comprises the step of removing the unreacted fluorine ion, other dissolved salts and residual organic matter contained in the treated water from which the organic matter was removed using a reverse osmosis membrane to discharge the reused treated water. Way. 제1항에 있어서, 상기 불산 폐수의 pH를 조정하는 단계는 불산 폐수의 pH가 5.0 내지 7.5가 되도록 조정하는 것임을 특징으로 하는 불산 폐수 처리 및 재이용 방법.According to claim 1, wherein the step of adjusting the pH of the hydrofluoric acid wastewater hydrofluoric acid wastewater treatment and reuse method, characterized in that for adjusting the pH of the hydrofluoric acid wastewater is 5.0 to 7.5. 불산을 포함하는 폐수 처리 및 재이용 장치에 있어서,In the wastewater treatment and reuse apparatus containing hydrofluoric acid, 응집제를 사용하여 불산 폐수의 pH를 조정하고, 산폐수에 포함된 불소 이온을 고형화된 불소화합물화하고 응집보조제에 의하여 형성된 고형물을 조대화하는 응집반응조;An agglomeration reaction tank which adjusts the pH of the hydrofluoric acid wastewater using a flocculant, solidifies the fluorine ions contained in the acid wastewater, and coarsens the solids formed by the flocculating aid; 상기 응집반응조에 의하여 조대화된 고형물을 정밀여과에 의하여 분리하여 탁도성분을 포함하는 고형물과 고형물이 제거된 처리수를 배출하는 정밀여과기;A fine filter for separating the solid coarse by the coagulation reaction tank by fine filtration to discharge the solids containing the turbidity component and the treated water from which the solids are removed; 상기 정밀여과기에 의하여 배출되는 처리수에 포함된 유기물을 활성탄을 이용하여 흡착하여 제거하는 활성탄흡착기; 및Activated carbon adsorber for removing the organic matter contained in the treated water discharged by the precision filter by using the activated carbon; And 상기 활성탄흡착기에 의하여 유기물이 제거된 처리수에 포함된 미반응 불소이온, 기타 용존염 및 잔류 유기물을 역삼투막을 이용하여 제거하여 재이용 가능한 처리수를 배출하는 역삼투기를 포함하는 것임을 특징으로 하는 불산 폐수 처리 장치.Foshan wastewater, characterized in that it comprises a reverse osmosis to remove the unreacted fluorine ions, other dissolved salts and residual organic matter contained in the treated water by the activated carbon adsorber using a reverse osmosis membrane to discharge the reused treated water Processing unit.
KR1019970015551A 1997-04-25 1997-04-25 Wastewater Treatment and Reuse Method using Microfiltration and Reverse Osmosis Membrane and Its Apparatus KR100193785B1 (en)

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KR101065940B1 (en) 2010-12-23 2011-09-19 그린엔텍 주식회사 Treatment and reuse system for wastewater containing high concentrations of hydrofluoric acid, phosphoric acid and nitric acid
KR20190129631A (en) * 2018-05-11 2019-11-20 삼성엔지니어링 주식회사 Method and apparatus for reusing hydrofluoric acid wastewater
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KR20030004662A (en) * 2001-07-06 2003-01-15 (주)에코 멤브레인 system for refiltering a filtered waste water
KR100790370B1 (en) * 2006-11-09 2008-01-02 주식회사 에스씨티 Recycling method and apparatus of waste etching solution
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KR101065940B1 (en) 2010-12-23 2011-09-19 그린엔텍 주식회사 Treatment and reuse system for wastewater containing high concentrations of hydrofluoric acid, phosphoric acid and nitric acid
KR20190129631A (en) * 2018-05-11 2019-11-20 삼성엔지니어링 주식회사 Method and apparatus for reusing hydrofluoric acid wastewater
KR102067164B1 (en) * 2018-05-11 2020-01-16 삼성엔지니어링 주식회사 Method and apparatus for reusing hydrofluoric acid wastewater
US11945744B2 (en) 2022-07-29 2024-04-02 Samsung Engineering Co., Ltd. Method and apparatus for reusing wastewater

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