KR100790370B1 - Recycling method and apparatus of waste etching solution - Google Patents
Recycling method and apparatus of waste etching solution Download PDFInfo
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- KR100790370B1 KR100790370B1 KR1020060110489A KR20060110489A KR100790370B1 KR 100790370 B1 KR100790370 B1 KR 100790370B1 KR 1020060110489 A KR1020060110489 A KR 1020060110489A KR 20060110489 A KR20060110489 A KR 20060110489A KR 100790370 B1 KR100790370 B1 KR 100790370B1
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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
- C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
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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
- C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable 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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/346—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from semiconductor processing, e.g. waste water from polishing of wafers
Abstract
Description
도 1은 본 발명의 폐에칭액의 재생 공정도 1 is a regeneration process chart of the waste etching solution of the present invention
<도면의 부호설명><Description of the Drawings>
폐에칭액저장탱크(1), 마이크로필터(2), 나노필터(3), 혼합탱크(4), 재생에칭액저장탱크(5), 폐에칭액공급관(10), 폐회수처리관(20), 질산공급관(30), 염산공급관(40), 에칭액회수관(50),Waste etching liquid storage tank (1), micro filter (2), nano filter (3), mixing tank (4), recycled etching liquid storage tank (5), waste etching liquid supply pipe (10), waste recovery treatment pipe (20), nitric acid supply pipe (30), hydrochloric acid supply pipe (40), etching liquid recovery pipe (50),
본 발명은 마이크로필터와 나노필터를 이용하여 에칭공정에서 사용된 후, 버려지는 폐에칭액의 재생장치 및 그 재생방법에 관한 것이다.The present invention relates to an apparatus for recycling waste etching liquid which is discarded after being used in an etching process using a microfilter and a nanofilter, and a method for regenerating the same.
반도체 및 PCB, LCD 제조 공정등에서 에칭(식각)공정이란 회로패턴을 형성시켜주기 위해 화학물질이나 반응성 가스를 사용하여 필요 없는 부분을 선택적으로 제거하는 공정으로서, 공업용 금속 에칭액으로 광범위하게 사용되어 오고 있다. 그러나 상기 성분으로 조성된 에칭액은 매우 강산이므로 에칭 후 잔류되는 에칭액은 환경에 매우 유해하여 반드시 중화시켜 처리해야 하며, 그 처리가 매우 어려우며, 처리비용이 고가이어서 이를 재활용하고자 많은 연구가 있어 왔다.The etching (etching) process in semiconductor, PCB, and LCD manufacturing processes is a process of selectively removing unnecessary parts by using chemicals or reactive gases to form circuit patterns, and has been widely used as an industrial metal etching solution. . However, since the etchant composed of the above components is very strong acid, the etchant remaining after the etching is very harmful to the environment and must be neutralized to be treated. The treatment is very difficult, and the processing cost is high, and there have been many studies to recycle it.
예를 들면, 국내공개특허공보 공개번호 제10-2004-25583호에는 에칭조에 있어서, 질화규소막을 에칭하기 위해 사용한 인산수용액으로 이루어지는 에칭액을 재생하는 방법에 있어서, 해당 에칭에 의해 발생하는 규소화합물을 포함하는 에칭액을 에칭조로부터 추출하고, 상기 추출한 에칭액에 물을 가하여, 해당 에칭액의 인산농도를 80~50중량%로 내리는 공정과, 해당 인산농도의 저하에 의해서 에칭액중에서 석출한 규소화합물을 에칭액으로부터 제거하는 공정인 에칭액의 재생방법, 에칭방법 및 에칭장치가 기재되어 있고,For example, Korean Laid-Open Patent Publication No. 10-2004-25583 discloses a method of regenerating an etching solution composed of an aqueous phosphate solution used to etch a silicon nitride film in an etching bath, wherein the silicon compound generated by the etching is included. The etching solution to be extracted from the etching bath, water was added to the extracted etching solution to lower the phosphoric acid concentration of the etching solution to 80 to 50% by weight, and the silicon compound precipitated in the etching solution by the decrease in the phosphoric acid concentration was removed from the etching solution. The etching method, the etching method and the etching apparatus are described
동 공보 공개번호 특2003-53247 및 특2003-532228호에는 알루미늄을 포함하는 폐황산에칭액 및 알루미늄을 포함하는 폐염산에칭액의 혼합액을 진공 증발시켜 염산을 회수하는 단계; 진공증발후 알루미늄을 포함하는 폐황산에칭액에 알루미늄을 첨가하는 단계, 상기 알루미늄이 첨가된 폐항산에칭액을 확산 투석하여 황산 및 황산알루미늄 수처리 응집제로 분리하는 단계를 포함하는 폐황산에칭액 및 폐염산에칭액의 재생방법이 기술되어 있으며,Publication Nos. 2003-53247 and 2003-532228 disclose the steps of recovering hydrochloric acid by vacuum evaporation of a mixed solution of waste sulfuric acid etchant comprising aluminum and waste hydrochloric acid etchant comprising aluminum; After the vacuum evaporation, adding aluminum to the waste sulfuric acid etching solution containing aluminum, the waste sulfuric acid etching solution and waste hydrochloric acid etching solution comprising the step of diffusing dialysis of the aluminum acid-added waste acid etching solution to the sulfuric acid and aluminum sulfate water treatment flocculant How to play it,
동 공보 공개번호 제10-2006-72559호에는 인디움주석산화물 에칭폐액을 마이크로필터로 여과하여 불용성 불순물을 제거하는 제1단계; 상기 제1단계 후, 상기 마이크로필터의 여액을 진공 증발하여 산을 회수하는 제2단계와, 상기 제2단계 후 잔류액을 전해 채취하여 인듐과 주석을 분리 회수하는 제3단계로 이루어진 인디움주석산화물 에칭폐액으로부터 산 회수 및 인듐, 주석을 회수하는 방법이 기재되어 있고,Publication No. 10-2006-72559 discloses a first step of filtering indium tin oxide etching waste liquid through a microfilter to remove insoluble impurities; After the first step, the indium tin comprises a second step of recovering the acid by vacuum evaporation of the filtrate of the microfilter, and a third step of separating and recovering indium and tin by electrolytically collecting the residual solution after the second step. A method for recovering acid and recovering indium and tin from an oxide etching waste liquid is described.
동 공보 공개번호 제10-2006-49695호에는 인디움주석산화물의 에칭에 사용한 옥살산 함유 에칭액을 나노필터막에 의해 여과하여 투과액과 비투과액으로 분리하는 여과공정으로 구성된 산성에칭액 재생방법 및 산성에칭액 재생장치가 기술되어있으며,Korean Patent Publication No. 10-2006-49695 discloses an acid etching solution regeneration method and an acid etching solution comprising a filtration process in which an oxalic acid-containing etching solution used for etching indium tin oxide is filtered by a nanofilter membrane and separated into a permeate solution and a non-permeate solution. A playback device is described,
동 공보 공개번호 제10-2006-11699호에는 인산을 함유하는 에칭폐액을 증류하여 인산만을 남기고 증류하는 단계, 희석물질로 희석하는 단계, 나노필터, 필요에 따라 킬레이트 수지 및 양이온 교환수지를 통과시켜 고순도의 인산을 제조하는 단계 및 에칭액으로 재생되는 단계로 구성된 알루미늄 에칭폐액 재생 및 인산의 고순도 정제방법이 공개되어 있으나,Publication No. 10-2006-11699 discloses a step of distilling an etching waste liquid containing phosphoric acid to distill leaving only phosphoric acid, diluting with diluent material, nanofilters, and optionally a chelating resin and a cation exchange resin. There is disclosed a method for regenerating aluminum etching waste liquid and refining phosphoric acid comprising the steps of preparing high purity phosphoric acid and regenerating with etching liquid.
상기와 같은 종래의 기술은 현재 공정상 한 번 사용한 에칭액은 전량 폐수처리장으로 이송되고 있어 폐수처리장의 부하증가와 에칭액을 제조를 위한 많은 비용이 들어가는 문제점이 있어 왔다.In the conventional technology as described above, the etching solution used once in the current process is transferred to the wastewater treatment plant, and thus, there is a problem in that the load of the wastewater treatment plant is increased and the cost for producing the etching solution is high.
상기와 같은 문제점을 해결하기 위하여 본 발명은 에칭액과 모재의 화학반응으로 모재에서 떨어져 나온 불용성 입자성분과 철, 구리, 아연, 비소, 납등의 금속이온(이하 "금속이온" 이라 함)을 제거하고, 초기 에칭액 성분인 순수, 질산, 염산 등을 회수하기 위한 시스템으로 마이크로필터와 나노필터, 혼합장치로 구성된 장치를 이용하여 에칭액을 재생하는 재생장치 및 그 재생방법을 제공하는 것이 본 발명이 이루고자 하는 기술적 과제인것이다.In order to solve the above problems, the present invention removes insoluble particle components and metal ions such as iron, copper, zinc, arsenic, and lead (hereinafter referred to as "metal ions") that are separated from the base material by chemical reaction between the etching solution and the base material. The present invention is to provide a regeneration apparatus for regenerating etching liquid using a device composed of a micro filter, a nano filter, and a mixing device as a system for recovering the initial etching liquid components, such as pure water, nitric acid, hydrochloric acid, and the like. It is a technical task.
상기 기술적 과제를 달성하기 위하여, 본 발명은 사용 후 폐기되는 에칭액을 1차 마이크로필터를 이용하여 불용성 입자성분을 제거한 후에, 고압펌프로 나노필터로 이송하여 금속이온 등을 제거하여 순수 및 질산, 염산 을 회수하여 이를 다시 사용하는 재생장치 및 그 재생방법에 관한 것이다.In order to achieve the above technical problem, the present invention is to remove the insoluble particle component by using the first micro-filter the etching liquid discarded after use, and then transferred to the nano-filter with a high-pressure pump to remove metal ions, etc. pure water, nitric acid, hydrochloric acid The present invention relates to a reproducing apparatus for recovering and using the same and to reusing the same.
본 발명에 사용되는 마이크로 필터는 여과분야에서 통상적으로 사용되는 마이크로필터를 사용한다.The micro filter used in the present invention uses a micro filter commonly used in the field of filtration.
현재 시판 중인 나노 필터를 사용할 수 있으며, 그 종류로는 Filmtec사 제조의 NF90-2540, NF90-4040, NF90-400, NF200-400, NF270-400, NF270-2540, NF270-4040, NF-400; Osmonics 사 제조의 CK2540FF, CK4040FF, CK8040F, CK8040N, Duraslick NF2540, Duraslick NF4040, Duraslick NF8040, HL2514T, HL2514TF, HL2540FF, HL2540TF, HL3218T, HL3308T, HL4014TF, HL4021TF, HL4040FF, HL4040FF-CERT, HL4040TF, HL8040F, HL8040F-400, HL8040N, DK2540F, DK4040F, DK8040F, DK2540C, DK4040C, DK8040C, DL2540F, DL4040F, DL8040F, DL2540C, DL4040C, DL8040C, Duracid NF2540C, Duracid NF4040C, Duracid NF8040C등을 들 수 있다.Nano-filters currently available can be used, and the types thereof include NF90-2540, NF90-4040, NF90-400, NF200-400, NF270-400, NF270-2540, NF270-4040, and NF-400 manufactured by Filmtec; CK2540FF, CK4040FF, CK8040F, CK8040N, Duraslick NF2540, Duraslick NF4040, Duraslick NF8040, HL2514T, HL2514TF, HL2540FF, HL2540TF, HL4018F, HL3FFT, HL4014TF, HL4014TF , HL8040N, DK2540F, DK4040F, DK8040F, DK2540C, DK4040C, DK8040C, DL2540F, DL4040F, DL8040F, DL2540C, DL4040C, DL8040C, Duracid NF2540C, Duracid NF4040C, Duracid NF8040C etc.
나노 필터는 약 0.001~0.01 마이크론의 기공 크기를 가지며, 원자량이 약 200이상인 물질들을 여과 제거하는데 사용될 수 있으나, 아직 일반화되어 있지는 않다. 최근, 나노 기술의 개발에 따라, 정밀 화학 분야의 분리/농축 공정과 연수화 공정에서 나노 필터의 사용이 증가하고 있는 추세이며, 염료, 안료 제조 공정에서 사용되는 다량의 염을 정제 공정에서 효과적으로 분리시키는 데에도 나노필터 막이 사용되고 있다. 또한, 분자량이 작은 의약품, 염료 등의 정제에도 나노필터가 적극 사용되고 있다.Nanofilters have a pore size of about 0.001 to 0.01 microns and can be used to filter out materials with atomic weights above about 200, but are not yet common. Recently, with the development of nanotechnology, the use of nanofilters in the separation / concentration process and water softening process in the fine chemical field is increasing, and a large amount of salts used in dye and pigment manufacturing processes are effectively separated from the purification process. Nanofilter membranes have also been used to make them. In addition, nanofilters are actively used for the purification of small pharmaceuticals, dyes and the like.
본 발명의 나노필터는 60℃에서 견딜 수 있는 재질로서, 폴리에테르설폰(PES), 폴리설폰등의 내산성이 높은 재질을 이용할 수 있으며, Nano-filter of the present invention as a material that can withstand at 60 ℃, it is possible to use a high acid resistance material, such as polyether sulfone (PES), polysulfone,
일측에 형성된 펌프에 의해 마이크로필터에서 공급된 폐에칭액 공급압력을 고압(약 10~30kgf/㎠)으로 공급할 수 있다.The waste etching solution supply pressure supplied from the micro filter by the pump formed on one side may be supplied at a high pressure (about 10 to 30 kgf / cm 2).
본 발명의 폐에칭액의 조성물은 순수:90% 이상, 질산:2~8%, 염산:0.1~1%, 불용성 입자성분과 10~수천ppm의 금속이온 등이며,The composition of the waste etching solution of the present invention is pure water: 90% or more, nitric acid: 2-8%, hydrochloric acid: 0.1-1%, insoluble particle component and 10-1000 ppm of metal ions,
최종회수된 폐에칭액 조성물 중 질산:1.8~7.6%, 염산:0.09~0.9% 를 회수하여 재사용하도록 개발한 것이다.It was developed to recover and reuse nitric acid: 1.8 ~ 7.6%, hydrochloric acid: 0.09 ~ 0.9% in the final recovered waste etching solution composition.
이하 본 발명을 실시예를 통하여 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to the following Examples.
실시예Example
제1공정(마이크로필터링 공정)First process (micro filtering process)
순수 90kg, 질산 8kg, 염산 1kg, 불용성입자와 금속이온 등으로 조성된 폐에칭액이 저장된 폐에칭액저장탱크(1)에서 펌프에 의해 마이크로필터(2)로 공급을 하면 불용성 입자성분은 걸러지고, 나머지 성분은 통과를 하게 되고, In the waste etching solution storage tank (1) containing 90 kg of pure water , 8 kg of nitric acid, 1 kg of hydrochloric acid, insoluble particles and metal ions, and supplied to the micro filter (2) by a pump, the insoluble particles are filtered out. The ingredients pass through,
제2공정(회수 공정)2nd process (recovery process)
상기 마이크로필터(2)에서 1차 처리된 폐에칭액을 펌프에 의해 폐에칭액 공급압력을 고압(약 10~30kgf/㎠)으로 나노필터(3)로 공급하여 금속이온 등을 제거하여 혼합탱크(4)로 이송한 다음, 하부일측에는 폐회수처리관(20)을 통해 금속 이온 등이 고농도로 함유된 폐액을 배출시키고, The waste etching solution first treated in the
제3공정(재생 공정)3rd process (regeneration process)
상기 나노필터(3)에서 회수된 에칭액이 혼합탱크(4) 로 이송되면, 내부에 설치된 센서를 이용하여, 일측 설치된 질산공급관(30) 및 염산공급관(40) 을 통해 질산과 염산이 공급되며, 하부에 설치된 펌프에 의해 재생에칭액저장탱크(5)로 이송 시킨 다음, 재생에칭액저장탱크(5)의 하부에 연결 설치된 에칭액회수관(50)을 통해 재사용하도록 폐에칭액을 재생하였다.When the etching liquid recovered from the nano-
이하, 첨부된 도면을 참조하여 본 고안의 바람직한 실시예를 상세히 설명한다.Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the accompanying drawings.
도 1은 본 발명의 폐에칭액의 재생 공정도, 폐에칭액저장탱크(1), 마이크로필터(2), 나노필터(3), 혼합탱크(4), 재생에칭액저장탱크(5), 폐에칭액공급관(10), 폐회수처리관(20), 질산공급관(30), 염산공급관(40), 에칭액회수관(50)을 나타낸 것임을 알 수 있다. 1 is a process for regenerating waste etching liquid of the present invention, waste etching liquid storage tank (1), micro filter (2), nano filter (3), mixing tank (4), regeneration etching liquid storage tank (5), waste etching liquid supply pipe (10), the
구조를 살펴보면 도 1에 도시된 바와 같이, 사용된 에칭액을 폐에칭액공급관(10)에 의해 연결되어 저장하는 폐에칭액저장탱크(1)와, 상기 폐에칭액저장탱크(1)에서 펌프에 의해 공급되어 처리하는 마이크로필터(2)와, 상기 마이크로필터(2)에서 1차 처리된 폐에칭액을 펌프에 의해 공급되어 2차 처리하며 하부 일측에는 폐회수처리관(20)이 구비된 나노필터(3)와, 상기 나노필터(3)에서 처리된 액을 저장하도록 연결되며, 다른 일측에는 질산공급관(30) 및 염산공급관(40) 이 연결된 혼합탱크(4)와, 상기 혼합탱크(4)에 연결된 재생된 에칭액을 저장하며, 다른 일측에는 에칭액회수관(50)이 구비된 재생에칭액저장탱크(5)로 구성된 폐에칭액의 재생장치인것이다.Looking at the structure, as shown in Figure 1, the waste etching liquid storage tank (1) for connecting and storing the used etching liquid by the waste etching
상술한 바와 같이, 본 발명은 마이크로필터, 나노필터를 이용하여 단시간 내에 연속적으로 폐에칭액을 처리하여 고순도로 재생된 질산, 염산을 재활용하는 경제적인 효과뿐만 아니라 폐수 발생량을 최소화하는 친환경적인 장점이 있는 것이다.As described above, the present invention has an eco-friendly advantage of minimizing waste water generation as well as the economic effect of recycling the recycled nitric acid and hydrochloric acid with high purity by treating the waste etching solution continuously within a short time using a micro filter and a nano filter. will be.
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