WO2017057883A1 - System for managing quality of paint for electrodeposition, and method for managing quality of paint for electrodeposition using same - Google Patents

System for managing quality of paint for electrodeposition, and method for managing quality of paint for electrodeposition using same Download PDF

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Publication number
WO2017057883A1
WO2017057883A1 PCT/KR2016/010760 KR2016010760W WO2017057883A1 WO 2017057883 A1 WO2017057883 A1 WO 2017057883A1 KR 2016010760 W KR2016010760 W KR 2016010760W WO 2017057883 A1 WO2017057883 A1 WO 2017057883A1
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paint
resin
electrodeposition
quality control
quality
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PCT/KR2016/010760
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French (fr)
Korean (ko)
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김선영
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대영엔지니어링 주식회사
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    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D5/00Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes
    • C09D5/44Coating compositions, e.g. paints, varnishes or lacquers, characterised by their physical nature or the effects produced; Filling pastes for electrophoretic applications
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D13/00Electrophoretic coating characterised by the process
    • C25D13/04Electrophoretic coating characterised by the process with organic material
    • C25D13/06Electrophoretic coating characterised by the process with organic material with polymers
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D13/00Electrophoretic coating characterised by the process
    • C25D13/22Servicing or operating apparatus or multistep processes

Definitions

  • the present invention relates to an electrodeposition coating quality management system and an electrodeposition coating quality management method using the same.
  • Coating is used for electrodeposition coating, and as the electrodeposition coating proceeds, the quality of the paint decreases, and various appearance defects occur in the electrodeposition coating.
  • the present invention provides an electrodeposition coating quality management system excellent in quality control and an electrodeposition coating quality management method using the same.
  • An object of the present invention is the electrodeposition coating paint quality management system, the electrodeposition coating is electrodeposited coating is immersed electrodeposition and the coating is accommodated; An ion resin portion in fluid communication with the electrodeposition tank and including the cation resin and the anion resin; It is achieved by including a control unit for controlling the operation of the electrodeposition tank and the ion resin unit.
  • the paint may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal.
  • the ion resin unit may include an anion resin unit including the anion resin and a cation resin unit including the cationic resin.
  • the electrodeposition tank, the anion resin portion, the cation resin portion may be connected in series and the anion resin portion may be directly connected to the electrodeposition tank.
  • the anion resin may be a strong base anion resin based on styrene-divinylbenzene.
  • the cation exchange resin may comprise a carboxylated polyacrylate.
  • the control unit may pass the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
  • the control unit may pass the paint through the cationic resin so that the amine equivalent (meq) of the paint is lower than a predetermined value.
  • the controller may pass the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
  • the method may further include an anion resin regeneration unit including a sodium hydroxide solution for regenerating the anion resin.
  • a cationic resin regeneration unit including an ammonia solution and a hydrochloric acid solution for regenerating the cationic resin may be further included.
  • An object of the present invention is a quality control method of the paint used for electrodeposition coating, the step of checking the physical properties of the paint; Determining whether the paint passes through the ion resin according to the identified physical properties; According to the determination may include passing the paint through the ion resin.
  • the paint may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal.
  • the ion resin may include an anion resin and a cationic resin.
  • the quality includes conductivity, and may include passing the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
  • the quality includes an amine equivalent (meq), and the paint may be passed through the cationic resin so that the amine equivalent of the paint is lower than a predetermined value.
  • the quality includes a pH, and may include passing the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
  • an electrodeposition coating quality management system excellent in quality control and an electrodeposition coating quality management method using the same According to the present invention, there is provided an electrodeposition coating quality management system excellent in quality control and an electrodeposition coating quality management method using the same.
  • FIG. 1 shows an electrodeposition coating quality management system according to an embodiment of the present invention
  • Figure 2 shows the electrical conductivity management flow chart of the tank paint according to an embodiment of the present invention
  • Figure 3 shows an amine equivalent management flowchart of the electrodeposition coating according to an embodiment of the present invention
  • Figure 4 shows the pH management flow chart of the electrodeposition coating according to an embodiment of the present invention.
  • FIG 1 shows an electrodeposition coating quality management system according to an embodiment of the present invention.
  • the paint quality management system 1 includes an electrodeposition tank 10, an ion resin unit 20, and a regeneration unit 30 in which paint is placed and electrodeposition coating is performed.
  • the paint moves the electrodeposition tank 10 and the ion resin portion 20, which is controlled by a controller (not shown).
  • the control unit may include a pump and a valve to control the transfer of paint.
  • the pipe is connected between the electrodeposition tank 10 and the ion resin portion 20.
  • the regeneration unit 30 includes a first regeneration unit 31 for regenerating the anion resin unit 21 and a second regeneration unit 32 for regenerating the cation resin unit 22.
  • the quality control target paint of the present invention is not limited thereto, but may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal.
  • a carboxylic acid may be attached to the acrylic resin terminal.
  • the weight of the paint located in the electrodeposition tank 10 during the electrodeposition process is not limited thereto, and may be 5 to 10 tons or more, for example, 10 to 15 tons, 10 to 20 tons, or 10 tons. It may be 50 tons.
  • Paint according to the invention can be used for transparent electrodeposition coating of a variety of materials, such as stainless steel, aluminum, iron.
  • the ion resin unit 20 includes an anion resin unit 21 and a cationic resin unit 22.
  • the anion resin part 21 and the cation resin part 22 are connected in series with the electrodeposition tank 10.
  • the electrodeposition tank 10 may be independently connected through separate pipes.
  • the anion resin unit 21 is a tower-type reactor is filled with anion resin inside.
  • the anion resin may be a strong base anion resin based on styrene-divinylbenzene, but is not limited thereto, and may use TRILITE-SAR20MB.
  • the cation resin part 22 is also a tower type reactor, and the cation resin is filled therein.
  • the cationic resin may be a carboxylated polyacrylate series, for example, WK60L may be used.
  • control unit manages the physical properties of the paint by passing the paint through the anion resin unit 21 and / or the cation resin unit 22.
  • the physical properties of the paint are not limited thereto, and may include electrical conductivity, amine equivalent weight and pH.
  • Figure 2 is a flow chart for managing the conductivity of the electrodeposition coating paint in one embodiment of the present invention
  • Figure 3 is a flow chart for managing the amine equivalent of the electrodeposition coating paint in one embodiment of the present invention
  • Figure 4 In one embodiment of the flow chart for managing the pH of the electrodeposition coating.
  • FIG. 2 describes the conductivity management of the paint.
  • impurities (cationic ions) in the pretreatment bath flow into the electrodeposition bath and conductivity increases. If the conductivity is excessively increased, the film thickness decreases, and if the conductivity is excessively reduced, the stability of the paint decreases.
  • the pretreatment tank is a process of surface treatment of the product before coating the product (electrodeposition object), there may be a degreasing process for removing oil or foreign matter and a chemical conversion process for improving corrosion resistance.
  • the conductivity of the paint increases, so the upper limit of the conductivity of the paint should be determined and managed so that the conductivity becomes lower than the upper limit. To prevent the conductivity of the paint from lowering below the lower limit, replenish the paint.
  • "managing a specific physical property (lower than a certain numerical value)” includes various control methods. For example, it is possible to always control the specific property to be located within a specific range (management range), or to start management if the specific value is exceeded (the specific value may be lower than the upper limit).
  • the upper limit and the lower limit of the specific range (control range), specifically, the physical property to be managed may vary depending on the specific process environment and / or required quality.
  • the conductivity of the paint is measured (S11).
  • the conductivity of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method.
  • the conductivity of the paint can be measured at all times or at regular time intervals.
  • the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
  • the measured value is a level that requires management (S12).
  • various conventional judgment methods may be used, such as viewing and predicting a change in conductivity of the paint over time.
  • the amine equivalent of the paint increases, so the upper limit of the amine equivalent of the paint should be determined and managed so that the amine equivalent is lower than the upper limit. To prevent the amine equivalent of the paint from lowering the lower limit, amine is replenished.
  • the amine equivalent of the paint is measured (S21).
  • the amine equivalent of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method.
  • the amine equivalent of the paint can be measured at all times or at regular time intervals.
  • the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
  • the measured value is a level that requires management (S22).
  • various conventional judgment methods can be used, such as predicting and predicting changes in amine equivalents of the paint over time.
  • the pH of the paint increases, so the pH upper limit of the paint must be determined and the pH lower than the upper limit should be managed.
  • amine may be replenished.
  • the pH of the paint is measured (S31).
  • the amine equivalent of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method.
  • the amine equivalent of the paint can be measured at all times or at regular time intervals.
  • the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
  • the measured value is a level that requires management (S32).
  • various conventional judgment methods may be used, such as viewing and predicting the pH change of the paint over time.
  • the management is determined to be necessary level to allow the paint in the electrodeposition tank 10 to pass through the cation resin (S33).
  • the paint passes through the cationic resin, and the pH is lowered while the weakly alkaline anions such as amines are substituted.
  • the passage of the ion resin of the paint may be stopped.
  • Ion resins can also be recycled if necessary.
  • the anion resin is regenerated using a regeneration solution containing a sodium hydroxide solution using the first regeneration unit 31, and the cation resin is regeneration solution containing an ammonia solution and a hydrochloric acid solution using the second regeneration unit 32. Can be played using.
  • the present invention when the line operation is close to the upper and lower limit limits, it is possible to take preliminary measures and analyzes according to expectations. In addition, it is possible to efficiently operate the paint and line according to the trend of production output. At the same time, it is possible to quickly identify and cope with the occurrence of a problem, to efficiently operate raw materials, and to increase productivity by managing a defective rate.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
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Abstract

The present invention relates to a system for managing the quality of a paint for electrodeposition, and a method for managing the quality of a paint for electrodeposition using the same. The system for managing the quality of a paint for electrodeposition according to the present invention comprises: an electrodeposition bath in which an object to be electrodeposited is immersed and electrodeposited, and a paint is accommodated; an ion resin part which is in fluid communication with the electrodeposition bath and comprises a cation resin and an anion resin; and a control part which controls the operation of the ion resin part and the electrodeposition bath.

Description

전착도장 도료품질관리시스템 및 이를 이용한 전착도장 도료품질관리방법Electrodeposition Coating Quality Management System and Electrodeposition Coating Quality Management Method Using the Same
본 발명은 전착도장 도료품질관리시스템 및 이를 이용한 전착도장 도료품질관리방법에 관한 것이다.The present invention relates to an electrodeposition coating quality management system and an electrodeposition coating quality management method using the same.
전착도장에는 도료가 사용되며, 전착도장이 진행됨에 따라 도료의 품질이 저하되어 전착도장되는 제품에 각종 외관불량이 발생한다.Coating is used for electrodeposition coating, and as the electrodeposition coating proceeds, the quality of the paint decreases, and various appearance defects occur in the electrodeposition coating.
작은 용량의 설비에서는 도료의 품질이 저하되면 폐기처분한다. 그런데, 폐기처분에 의해 도료 비용이 증가하는 문제가 발생한다. 특히 큰 용량의 설비에서는 도료의 사용량이 많기 때문에 폐기처분의 방식을 사용하면 원가가 크게 증가하게 된다.In small-capacity installations, the paint quality is disposed of and discarded. However, a problem arises in that the paint cost increases due to disposal. In particular, large-capacity equipment uses a lot of paint, so the cost of disposal is greatly increased.
본 발명은 품질관리가 우수한 전착도장 도료품질관리시스템 및 이를 이용한 전착도장 도료품질관리방법을 제공하는 것이다.The present invention provides an electrodeposition coating quality management system excellent in quality control and an electrodeposition coating quality management method using the same.
상기 본 발명의 목적은 전착도장 도료품질관리시스템에 있어서, 피전착도장물이 침지되어 전착되며 도료가 수용되는 전착조와; 상기 전착조와 유체소통되며 상기 양이온수지와 음이온수지를 포함하는 이온수지부와; 상기 전착조와 상기 이온수지부의 운전을 제어하는 제어부를 포함하는 것에 의해 달성된다.An object of the present invention is the electrodeposition coating paint quality management system, the electrodeposition coating is electrodeposited coating is immersed electrodeposition and the coating is accommodated; An ion resin portion in fluid communication with the electrodeposition tank and including the cation resin and the anion resin; It is achieved by including a control unit for controlling the operation of the electrodeposition tank and the ion resin unit.
상기 도료는 아크릴 수지와 멜라닌 수지를 포함하며 아크릴 수지 말단에 카르복실산이 부착되어 있을 수 있다.The paint may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal.
상기 이온수지부는 상기 음이온수지를 포함하는 음이온수지부와 상기 양이온수지를 포함하는 양이온수지부를 포함할 수 있다.The ion resin unit may include an anion resin unit including the anion resin and a cation resin unit including the cationic resin.
상기 전착조, 상기 음이온수지부, 상기 양이온수지부는 직렬로 연결되어 있으며 상기 음이온수지부가 상기 전착조에 직접 연결되어 있을 수 있다.The electrodeposition tank, the anion resin portion, the cation resin portion may be connected in series and the anion resin portion may be directly connected to the electrodeposition tank.
상기 음이온수지는 스타이렌-디비닐벤젠을 기본 모체로 하는 강염기성 음이온수지일 수 있다.The anion resin may be a strong base anion resin based on styrene-divinylbenzene.
상기 양이온교환수지는 카르복실산화된 폴리아크릴레이트를 포함할 수 있다.The cation exchange resin may comprise a carboxylated polyacrylate.
상기 제어부는 상기 도료의 전도도가 일정수치보다 낮아지도록 상기 도료를 상기 음이온수지에 통과시킬 수 있다.The control unit may pass the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
상기 제어부는 상기 도료의 아민당량(meq)이 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시킬 수 있다.The control unit may pass the paint through the cationic resin so that the amine equivalent (meq) of the paint is lower than a predetermined value.
상기 제어부는 상기 도료의 pH가 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시킬 수 있다.The controller may pass the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
상기 음이온수지를 재생하기 위한 수산화나트륨 용액을 포함하는 음이온수지재생부를 더 포함할 수 있다.The method may further include an anion resin regeneration unit including a sodium hydroxide solution for regenerating the anion resin.
상기 양이온수지를 재생하기 위한 암모니아 용액과 염산용액을 포함하는 양이온수지재생부를 더 포함할 수 있다.A cationic resin regeneration unit including an ammonia solution and a hydrochloric acid solution for regenerating the cationic resin may be further included.
상기 본 발명의 목적은 전착도장에 사용되는 도료의 품질관리방법에 있어서, 상기 도료의 물성을 확인하는 단계와; 확인된 물성에 따라서 상기 도료의 이온수지통과여부를 결정하는 단계와; 상기 결정에 따라 상기 도료를 이온수지에 통과시키는 단계를 포함할 수 있다.An object of the present invention is a quality control method of the paint used for electrodeposition coating, the step of checking the physical properties of the paint; Determining whether the paint passes through the ion resin according to the identified physical properties; According to the determination may include passing the paint through the ion resin.
상기 도료는 아크릴 수지와 멜라닌 수지를 포함하며 아크릴 수지 말단에 카르복실산이 부착되어 있을 수 있다.The paint may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal.
상기 이온수지는 음이온수지와 양이온수지를 포함할 수 있다.The ion resin may include an anion resin and a cationic resin.
상기 품질은 전도도를 포함하며, 상기 도료의 전도도가 일정수치보다 낮아지도록 상기 도료를 상기 음이온수지에 통과시키는 단계를 포함할 수 있다. The quality includes conductivity, and may include passing the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
상기 품질은 아민당량(meq)을 포함하며, 상기 도료의 아민당량이 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시킬 수 있다.The quality includes an amine equivalent (meq), and the paint may be passed through the cationic resin so that the amine equivalent of the paint is lower than a predetermined value.
상기 품질은 pH를 포함하며, 상기 도료의 pH가 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시키는 단계를 포함할 수 있다. The quality includes a pH, and may include passing the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
본 발명에 따르면 품질관리가 우수한 전착도장 도료품질관리시스템 및 이를 이용한 전착도장 도료품질관리방법이 제공된다.According to the present invention, there is provided an electrodeposition coating quality management system excellent in quality control and an electrodeposition coating quality management method using the same.
도 1은 본 발명의 일실시예에 따른 전착도장 도료품질관리 시스템을 나타낸 것이고,1 shows an electrodeposition coating quality management system according to an embodiment of the present invention,
도 2는 본 발명의 일실시예에 따른 전차도장 도료의 전기전도도 관리 순서도를 나타낸 것이고,Figure 2 shows the electrical conductivity management flow chart of the tank paint according to an embodiment of the present invention,
도 3은 본 발명의 일실시예에 따른 전착도장 도료의 아민당량 관리 순서도를 나타낸 것이고,Figure 3 shows an amine equivalent management flowchart of the electrodeposition coating according to an embodiment of the present invention,
도 4는 본 발명의 일실시예에 따른 전착도장 도료의 pH 관리 순서도를 나타낸 것이다. Figure 4 shows the pH management flow chart of the electrodeposition coating according to an embodiment of the present invention.
도 1은 본 발명의 일실시예에 따른 전착도장 도료품질관리 시스템을 나타낸 것이다.1 shows an electrodeposition coating quality management system according to an embodiment of the present invention.
도료품질관리 시스템(1)은 도료가 위치하게 되며 전착도장이 수행되는 전착조(10), 이온수지부(20) 및 재생부(30)를 포함한다. 도료는 전착조(10)와 이온수지부(20)를 이동하며, 이는 제어부(도시하지 않음)에 의해 제어된다. 제어부는 도료의 이송을 제어하기 위해 펌프와 밸브 등을 포함할 수 있다. 이 외에 번호를 부여하지는 않았지만 전착조(10)와 이온수지부(20) 사이를 연결하는 배관이 포함된다.The paint quality management system 1 includes an electrodeposition tank 10, an ion resin unit 20, and a regeneration unit 30 in which paint is placed and electrodeposition coating is performed. The paint moves the electrodeposition tank 10 and the ion resin portion 20, which is controlled by a controller (not shown). The control unit may include a pump and a valve to control the transfer of paint. In addition, although not given a number, the pipe is connected between the electrodeposition tank 10 and the ion resin portion 20.
재생부(30)는 음이온수지부(21)를 재생하는 제1재생부(31)와 양이온수지부(22)를 재생하는 제2재생부(32)를 포함한다.The regeneration unit 30 includes a first regeneration unit 31 for regenerating the anion resin unit 21 and a second regeneration unit 32 for regenerating the cation resin unit 22.
본 발명의 품질관리 대상 도료는, 이에 한정되지 않으나, 아크릴 수지와 멜라닌 수지를 포함하며 아크릴 수지 말단에 카르복실산이 부착되어 있을 수 있다. 이러한 음이온 순수 아크릭 전착수지를 사용하면 고광택과 메탈감을 얻을 수 있다. 전착공정 중 전착조(10)에 위치하는 도료의 무게는, 이에 한정되지 않으나, 5톤 이상이나 10톤 이상일 수 있으며, 예를 들어 10톤 내지 15톤, 10톤 내지 20톤, 또는 10톤 내지 50톤일 수 있다.The quality control target paint of the present invention is not limited thereto, but may include an acrylic resin and a melanin resin, and a carboxylic acid may be attached to the acrylic resin terminal. By using such anion pure acrylic electrodeposited resin, high gloss and a metallic feeling can be obtained. The weight of the paint located in the electrodeposition tank 10 during the electrodeposition process is not limited thereto, and may be 5 to 10 tons or more, for example, 10 to 15 tons, 10 to 20 tons, or 10 tons. It may be 50 tons.
본 발명에 따른 도료는 스테인레스, 알루미늄, 철 등 다양한 재질의 투명전착도장에 사용될 수 있다.Paint according to the invention can be used for transparent electrodeposition coating of a variety of materials, such as stainless steel, aluminum, iron.
이온수지부(20)는 음이온수지부(21)와 양이온수지부(22)를 포함한다. 음이온수지부(21)와 양이온수지부(22)는 전착조(10)와 직렬로 연결되어 있다. 다른 실시예에서는 전착조(10)에 각각 별도의 배관을 통해 독립적으로 연결될 수 있다. 도료의 운전은 음이온수지만을 통과시키거나, 음이온수지를 먼저 통과 후 양이온수지를 통과하는 것이 바람직하다. 이는 도료를 양이온수지만을 통과시키면 도료에 아민을 기준치 이상으로 치환할 가능성이 높아 도료 안정성에 문제가 발생할 수 있기 때문이다.The ion resin unit 20 includes an anion resin unit 21 and a cationic resin unit 22. The anion resin part 21 and the cation resin part 22 are connected in series with the electrodeposition tank 10. In another embodiment, the electrodeposition tank 10 may be independently connected through separate pipes. In the operation of the paint, it is preferable to pass only the anion resin, or pass the anion resin first and then the cationic resin. This is because if the paint passes through only the cationic resin, the paint may have a high probability of replacing the amine above the reference value, which may cause problems in the paint stability.
음이온수지부(21)는 탑형식의 반응기로 내부에 음이온수지가 충진되어 있다. 음이온수지는, 스타이렌-디비닐벤젠을 기본 모체로 하는 강염기성 음이온수지를 사용할 수 있으며, 이에 한정되지 않으나, TRILITE-SAR20MB를 사용할 수 있다. 양이온수지부(22) 역시 탑형식의 반응기로 내부에 양이온수지가 충진되어 있다. 양이온수지는, 카르복실산화된 폴리아크릴레이트계열일 수 있으며, 예를 들어 WK60L을 사용할 수 있다.The anion resin unit 21 is a tower-type reactor is filled with anion resin inside. The anion resin may be a strong base anion resin based on styrene-divinylbenzene, but is not limited thereto, and may use TRILITE-SAR20MB. The cation resin part 22 is also a tower type reactor, and the cation resin is filled therein. The cationic resin may be a carboxylated polyacrylate series, for example, WK60L may be used.
제어부는 도료의 물성을 관리할 필요가 있다고 판단되는 경우 도료를 음이온수지부(21) 및/또는 양이온수지부(22)를 통과시켜 도료의 물성을 관리한다. 도료의 물성은, 이에 한정되지 않으나, 전기전도도, 아민당량 및 pH를 포함할 수 있다.If it is determined that the physical properties of the paint need to be managed, the control unit manages the physical properties of the paint by passing the paint through the anion resin unit 21 and / or the cation resin unit 22. The physical properties of the paint are not limited thereto, and may include electrical conductivity, amine equivalent weight and pH.
이하에서는 전착도장 도료의 품질관리 방법을 도 2 내지 도 4를 참조하여 설명한다.Hereinafter, a quality control method of electrodeposition coating will be described with reference to FIGS. 2 to 4.
도 2는 본 발명의 일실시예에서 전착도장 도료의 전도도를 관리하기 위한 순서도이고, 도 3은 본 발명의 일실시예에서 전착도장 도료의 아민당량을 관리하기 위한 순서도이고, 도 4는 본 발명의 일실시예에서 전착도장 도료의 pH를 관리하기 위한 순서도이다.Figure 2 is a flow chart for managing the conductivity of the electrodeposition coating paint in one embodiment of the present invention, Figure 3 is a flow chart for managing the amine equivalent of the electrodeposition coating paint in one embodiment of the present invention, Figure 4 In one embodiment of the flow chart for managing the pH of the electrodeposition coating.
도 2를 참조하여 도료의 전도도 관리를 설명한다. Referring to Figure 2 describes the conductivity management of the paint.
전착도장이 진행되면 전처리조에 있던 불순물(양가이온)들이 전착조로 유입되어 전도도가 증가하게 된다. 전도도가 과도하게 증가하게 되면 도막두께가 감소하는 문제가 생기며, 전도도가 과도하게 감소하게 되면 도료의 안정성이 감소한다. As the electrodeposition coating proceeds, impurities (cationic ions) in the pretreatment bath flow into the electrodeposition bath and conductivity increases. If the conductivity is excessively increased, the film thickness decreases, and if the conductivity is excessively reduced, the stability of the paint decreases.
전처리조는 제품(전착도장 대상체)에 도료가 입혀지기 전에 제품의 표면처리를 하는 공정으로 유분이나 이물을 제거하는 탈지공정과 내식성 개선을 위한 화성피막공정이 있을 수 있다.The pretreatment tank is a process of surface treatment of the product before coating the product (electrodeposition object), there may be a degreasing process for removing oil or foreign matter and a chemical conversion process for improving corrosion resistance.
전착도장이 진행됨에 따라 도료의 전도도는 증가하므로, 도료의 전도도 상한값을 정하고 상한값보다 전도도가 낮아지도록 관리해야 한다. 도료의 전도도가 하한값보다 낮아지는 것을 방지하기 위해서는 도료를 보충한다.As the electrodeposition coating progresses, the conductivity of the paint increases, so the upper limit of the conductivity of the paint should be determined and managed so that the conductivity becomes lower than the upper limit. To prevent the conductivity of the paint from lowering below the lower limit, replenish the paint.
본 발명에서 "특정물성을 (일정수치보다 낮아지게) 관리"한다는 것은 다양한 제어방법을 포함한다. 예를 들어, 특정물성이 특정범위(관리범위) 내에 위치하도록 항시 제어하거나, 특정수치(특정수치는 상한값보다 낮을 수 있음)를 넘어가면 관리를 시작하는 방법 등이 가능하다. 여기서, 특정범위(관리범위), 구체적으로는 관리대상 물성의 상한값과 하한값은 특정한 공정환경 및/또는 요구품질 등에 따라 달라질 수 있다.In the present invention, "managing a specific physical property (lower than a certain numerical value)" includes various control methods. For example, it is possible to always control the specific property to be located within a specific range (management range), or to start management if the specific value is exceeded (the specific value may be lower than the upper limit). Here, the upper limit and the lower limit of the specific range (control range), specifically, the physical property to be managed may vary depending on the specific process environment and / or required quality.
구체적으로 보면, 먼저 도료의 전도도를 측정한다(S11). 도료의 전도도는, 이에 한정되지는 않으나, 전착조(10)내의 도료를 대상으로 측정할 수 있으며 공지의 방법으로 수행할 수 있다. 도료의 전도도는 항시 측정하거나 일정한 시간 간격으로 측정할 수 있다. 또한 특정범위(관리범위)의 상한값 또는 하한값에 근접하면 측정빈도를 증가시킬 수 있다.Specifically, first, the conductivity of the paint is measured (S11). The conductivity of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method. The conductivity of the paint can be measured at all times or at regular time intervals. In addition, the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
다음으로 측정된 값이 관리가 필요한 수준인지 판단한다(S12). 이 단계에서는 시간에 따른 도료의 전도도 변화추이를 보고 예측하는 등, 다양한 종래의 판단방법을 사용할 수 있다.Next, it is determined whether the measured value is a level that requires management (S12). In this step, various conventional judgment methods may be used, such as viewing and predicting a change in conductivity of the paint over time.
이후 관리가 필요한 수준으로 판단되면 전착조(10) 내의 도료가 음이온수지를 통과하도록 한다(S13). 이에 의해 도료가 음이온수지를 통과하면서 양가이온이 치환되어 전도도가 하락하게 된다.After the management is determined to be a necessary level to allow the paint in the electrodeposition tank 10 to pass through the anion resin (S13). As a result, as the paint passes through the anion resin, the cationic ions are substituted and the conductivity decreases.
다음으로 도 3을 참조하여 도료의 아민 당량 관리를 설명한다. Next, with reference to FIG. 3, the amine equivalent control of paint is demonstrated.
전착도장이 진행되면 아크릴 수지를 감싸고 있던 아민이 해리되어 전착조에 남아있게 된다. 이에 의해 도료의 아민당량이 증가하게 된다. 아민당량이 과도하게 높으면 전착레벨링이 감소하고 도막두께가 감소하는 문제가 생기며, 아민당량이 과도하게 낮으면 도료의 안정성이 감소하고 도막두께가 증가한다. 즉 아민당량의 도료의 평활성 관리에 중요하다. As the electrodeposition coating proceeds, the amines surrounding the acrylic resin dissociate and remain in the electrodeposition tank. This increases the amine equivalent weight of the paint. Excessively high amine equivalents result in a problem of reduced electrodeposition leveling and a decrease in coating thickness. Excessively low amine equivalents reduce paint stability and increase coating thickness. That is, it is important for the smoothness management of amine equivalent paint.
전착도장이 진행됨에 따라 도료의 아민당량은 증가하므로, 도료의 아민당량 상한값을 정하고 상한값보다 아민당량이 낮아지도록 관리해야 한다. 도료의 아민당량이 하한값보다 낮아지는 것을 방지하기 위해서는 아민을 보충한다.As the electrodeposition coating proceeds, the amine equivalent of the paint increases, so the upper limit of the amine equivalent of the paint should be determined and managed so that the amine equivalent is lower than the upper limit. To prevent the amine equivalent of the paint from lowering the lower limit, amine is replenished.
구체적으로 보면, 먼저 도료의 아민당량을 측정한다(S21). 도료의 아민당량은, 이에 한정되지는 않으나, 전착조(10)내의 도료를 대상으로 측정할 수 있으며 공지의 방법으로 수행할 수 있다. 도료의 아민당량은 항시 측정하거나 일정한 시간간격으로 측정할 수 있다. 또한 특정범위(관리범위)의 상한값 또는 하한값에 근접하면 측정빈도를 증가시킬 수 있다.Specifically, first, the amine equivalent of the paint is measured (S21). The amine equivalent of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method. The amine equivalent of the paint can be measured at all times or at regular time intervals. In addition, the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
다음으로 측정된 값이 관리가 필요한 수준인지 판단한다(S22). 이 단계에서는 시간에 따른 도료의 아민당량 변화추이를 보고 예측하는 등, 다양한 종래의 판단방법을 사용할 수 있다.Next, it is determined whether the measured value is a level that requires management (S22). In this step, various conventional judgment methods can be used, such as predicting and predicting changes in amine equivalents of the paint over time.
이후 관리가 필요한 수준으로 판단되면 전착조(10) 내의 도료가 양이온수지를 통과하도록 한다(S23). 이에 의해 도료가 양이온수지를 통과하면서 아민이 치환되면서 아민당량이 하락하게 된다.After the management is determined to be necessary level to allow the paint in the electrodeposition tank 10 to pass through the cation resin (S23). As the paint passes through the cationic resin, the amine is substituted and the amine equivalent decreases.
다음으로 도 4를 참조하여 도료의 pH 관리를 설명한다. Next, the pH control of the paint will be described with reference to FIG. 4.
전착도장이 진행되면 아크릴 수지를 감싸고 있던 아민과 같은 약알칼리를 띤 음가이온이 해리되어 전착조에 남아있게 된다. 이에 의해 도료의 pH가 상승하게 된다. pH 과도하게 높으면 도료의 안정성이 낮아지고 외관불량을 야기한다. pH가 과도하게 낮으면 역시 도료의 안정성이 낮아진다. As the electrodeposition coating progresses, weakly alkaline anions such as amines surrounding the acrylic resin dissociate and remain in the electrodeposition tank. This raises the pH of the paint. Excessively high pH lowers the stability of the paint and causes poor appearance. Too low a pH also lowers the stability of the paint.
전착도장이 진행됨에 따라 도료의 pH는 증가하므로, 도료의 pH 상한값을 정하고 상한값보다 pH가 낮아지도록 관리해야 한다. 도료의 pH이 하한값보다 낮아지는 것을 방지하기 위해서는 아민을 보충할 수 있다.As the electrodeposition coating proceeds, the pH of the paint increases, so the pH upper limit of the paint must be determined and the pH lower than the upper limit should be managed. In order to prevent the pH of the paint from lowering the lower limit, amine may be replenished.
구체적으로 보면, 먼저 도료의 pH를 측정한다(S31). 도료의 아민당량은, 이에 한정되지는 않으나, 전착조(10)내의 도료를 대상으로 측정할 수 있으며 공지의 방법으로 수행할 수 있다. 도료의 아민당량은 항시 측정하거나 일정한 시간간격으로 측정할 수 있다. 또한 특정범위(관리범위)의 상한값 또는 하한값에 근접하면 측정빈도를 증가시킬 수 있다.Specifically, first, the pH of the paint is measured (S31). The amine equivalent of the paint is not limited thereto, but may be measured for the paint in the electrodeposition tank 10 and may be performed by a known method. The amine equivalent of the paint can be measured at all times or at regular time intervals. In addition, the measurement frequency can be increased when the upper limit or the lower limit of a specific range (management range) is approached.
다음으로 측정된 값이 관리가 필요한 수준인지 판단한다(S32). 이 단계에서는 시간에 따른 도료의 pH 변화추이를 보고 예측하는 등, 다양한 종래의 판단방법을 사용할 수 있다.Next, it is determined whether the measured value is a level that requires management (S32). In this step, various conventional judgment methods may be used, such as viewing and predicting the pH change of the paint over time.
이후 관리가 필요한 수준으로 판단되면 전착조(10) 내의 도료가 양이온수지를 통과하도록 한다(S33). 이에 의해 도료가 양이온수지를 통과하면서 아민과 같은 약알칼리를 띤 음가이온이 치환되면서 pH가 하락하게 된다.After the management is determined to be necessary level to allow the paint in the electrodeposition tank 10 to pass through the cation resin (S33). As a result, the paint passes through the cationic resin, and the pH is lowered while the weakly alkaline anions such as amines are substituted.
이상 도 2 내지 도 4를 참조한 설명에서는 생략되었지만, 이온수지 통과를 통해 도료의 물성이 일정수치 내로 들어오면 도료의 이온수지 통과를 중단할 수 있다.Although not described above with reference to FIGS. 2 to 4, when the physical properties of the paint enter a predetermined value through the passage of the ion resin, the passage of the ion resin of the paint may be stopped.
또한 이온수지는 필요시 재생시킬 수 있다. 음이온수지는 제1재생부(31)를 이용하여 수산화나트륨 용액을 포함하는 재생용액을 이용하고 재생하고, 양이온수지는 제2재생부(32)를 이용하여 암모니아 용액과 염산용액을 포함하는 재생용액을 이용하여 재생할 수 있다.Ion resins can also be recycled if necessary. The anion resin is regenerated using a regeneration solution containing a sodium hydroxide solution using the first regeneration unit 31, and the cation resin is regeneration solution containing an ammonia solution and a hydrochloric acid solution using the second regeneration unit 32. Can be played using.
재생 공정의 필요성 및 구체적인 재생방법은 공지의 기술로 수행될 수 있다.The necessity of the regeneration process and the specific regeneration method can be carried out by known techniques.
본 발명에 따르면, 라인운용 중 상, 하한치 한도 근접 시 예상에 따른 선조치 및 분석이 가능해진다. 또한, 생산량 변동추이에 따른 도료 및 라인의 효율적인 운용이 가능해진다. 이와 함께, 문제발생에 따른 빠른 원인파악 및 대처가 가능하고, 원자재의 효율적 운용이 가능해지며, 불량률 관리에 의해 생산성이 증대된다.According to the present invention, when the line operation is close to the upper and lower limit limits, it is possible to take preliminary measures and analyzes according to expectations. In addition, it is possible to efficiently operate the paint and line according to the trend of production output. At the same time, it is possible to quickly identify and cope with the occurrence of a problem, to efficiently operate raw materials, and to increase productivity by managing a defective rate.
본 발명은 첨부된 도면에 도시된 일 실시예를 참고로 설명되었으나 이는 예시적인 것에 불과하며, 당해 기술분야에서 통상의 지식을 가진 자라면 이로부터 다양한 변형 및 균등한 타 실시예가 가능하다는 점을 이해할 수 있을 것이다. 따라서, 본 발명의 진정한 보호 범위는 첨부된 청구 범위에 의해서만 정해져야 할 것이다.Although the present invention has been described with reference to one embodiment shown in the accompanying drawings, this is merely exemplary, and it will be understood by those skilled in the art that various modifications and equivalent other embodiments are possible. Could be. Accordingly, the true scope of protection of the invention should be defined only by the appended claims.

Claims (17)

  1. 전착도장 도료품질관리시스템에 있어서,In electrodeposition coating quality management system,
    피전착도장물이 침지되어 전착되며 도료가 수용되는 전착조와;An electrodeposition tank in which the object to be electrodeposited is immersed and the paint is accommodated;
    상기 전착조와 유체소통되며 상기 양이온수지와 음이온수지를 포함하는 이온수지부와;An ion resin portion in fluid communication with the electrodeposition tank and including the cation resin and the anion resin;
    상기 전착조와 상기 이온수지부의 운전을 제어하는 제어부를 포함하는 전착도장 도료품질관리시스템.Electrodeposit coating quality control system including a control unit for controlling the operation of the electrodeposition tank and the ion resin.
  2. 제1항에 있어서, The method of claim 1,
    상기 도료는 아크릴 수지와 멜라닌 수지를 포함하며 아크릴 수지 말단에 카르복실산이 부착되어 있는 것을 특징으로 하는 전착도장 도료품질관리시스템.The paint includes an acrylic resin and a melanin resin, the electrodeposition coating quality management system, characterized in that the carboxylic acid is attached to the acrylic resin end.
  3. 제1항에 있어서, The method of claim 1,
    상기 이온수지부는 상기 음이온수지를 포함하는 음이온수지부와 상기 양이온수지를 포함하는 양이온수지부를 포함하는 것을 특징으로 하는 전착도장 도료품질관리시스템.Electrodeposit coating quality control system, characterized in that the ion resin portion comprises an anion resin portion including the anion resin and a cation resin portion containing the cation resin.
  4. 제3항에 있어서, The method of claim 3,
    상기 전착조, 상기 음이온수지부, 상기 양이온수지부는 직렬로 연결되어 있으며 상기 음이온수지부가 상기 전착조에 직접 연결되어 있는 것을 특징으로 하는 전착도장 도료품질관리시스템.Electrodeposit coating quality control system, characterized in that the electrodeposition tank, the anion resin portion, the cation resin portion is connected in series and the anion resin portion is directly connected to the electrodeposition tank.
  5. 제4항에 있어서,The method of claim 4, wherein
    상기 음이온수지는 스타이렌-디비닐벤젠을 기본 모체로 하는 강염기성 음이온수지인 것을 특징으로 하는 전착도장 도료품질관리시스템.Electrodeposit coating quality control system, characterized in that the anionic resin is a strong basic anion resin based on styrene-divinylbenzene.
  6. 제4항에 있어서,The method of claim 4, wherein
    상기 양이온교환수지는 카르복실산화된 폴리아크릴레이트를 포함하는 것을 특징으로 하는 전착도장 도료품질관리시스템.Electrodeposit coating quality management system, characterized in that the cation exchange resin comprises a carboxylated polyacrylate.
  7. 제4항에 있어서,The method of claim 4, wherein
    상기 제어부는 상기 도료의 전도도가 일정수치보다 낮아지도록 상기 도료를 상기 음이온수지에 통과시키는 것을 특징으로 하는 전착도장 도료품질관리시스템.And the control unit passes the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
  8. 제4항에 있어서,The method of claim 4, wherein
    상기 제어부는 상기 도료의 아민당량(meq)이 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시키는 것을 특징으로 하는 전착도장 도료품질관리시스템.And the control unit passes the paint through the cationic resin so that the amine equivalent (meq) of the paint is lower than a predetermined value.
  9. 제4항에 있어서,The method of claim 4, wherein
    상기 제어부는 상기 도료의 pH가 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시키는 것을 특징으로 하는 전착도장 도료품질관리시스템.The control unit is electrodeposition coating paint quality management system, characterized in that to pass the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
  10. 제4항에 있어서,The method of claim 4, wherein
    상기 음이온수지를 재생하기 위한 수산화나트륨 용액을 포함하는 음이온수지재생부를 더 포함하는 전착도장 도료품질관리시스템.Electrodeposit coating quality control system further comprising an anionic resin regeneration unit comprising a sodium hydroxide solution for regenerating the anionic resin.
  11. 제4항에 있어서,The method of claim 4, wherein
    상기 양이온수지를 재생하기 위한 암모니아 용액과 염산용액을 포함하는 양이온수지재생부를 더 포함하는 전착도장 도료품질관리시스템. Electrodeposit coating quality control system further comprising a cationic resin regeneration unit comprising ammonia solution and hydrochloric acid solution for regenerating the cationic resin.
  12. 전착도장에 사용되는 도료의 품질관리방법에 있어서,In the quality control method of the paint used for electrodeposition coating,
    상기 도료의 물성을 확인하는 단계와;Confirming physical properties of the paint;
    확인된 물성에 따라서 상기 도료의 이온수지통과여부를 결정하는 단계와;Determining whether the paint passes through the ion resin according to the identified physical properties;
    상기 결정에 따라 상기 도료를 이온수지에 통과시키는 단계를 포함하는 전착도장 도료의 품질관리방법.Quality control method of electrodeposition coating paint comprising the step of passing the paint through the ion resin according to the determination.
  13. 제12항에 있어서, The method of claim 12,
    상기 도료는 아크릴 수지와 멜라닌 수지를 포함하며 아크릴 수지 말단에 카르복실산이 부착되어 있는 것을 특징으로 하는 전착도장 도료의 품질관리방법.The paint includes an acrylic resin and a melanin resin, the quality control method of the electrodeposition coating paint, characterized in that the carboxylic acid is attached to the acrylic resin end.
  14. 제12항에 있어서, The method of claim 12,
    상기 이온수지는 음이온수지와 양이온수지를 포함하는 것을 특징으로 하는 전착도장 도료의 품질관리방법.The ion resin quality control method of the electrodeposition coating, characterized in that it comprises an anionic resin and a cationic resin.
  15. 제14항에 있어서,The method of claim 14,
    상기 품질은 전도도를 포함하며,The quality includes conductivity,
    상기 도료의 전도도가 일정수치보다 낮아지도록 상기 도료를 상기 음이온수지에 통과시키는 단계를 포함하는 것을 특징으로 하는 전착도장 도료의 품질관리방법.And passing the paint through the anion resin so that the conductivity of the paint is lower than a predetermined value.
  16. 제14항에 있어서,The method of claim 14,
    상기 품질은 아민당량(meq)을 포함하며,The quality comprises an amine equivalent (meq),
    상기 도료의 아민당량이 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시키는 것을 특징으로 하는 전착도장 도료의 품질관리방법.Quality control method of the electrodeposition coating paint, characterized in that the paint is passed through the cationic resin so that the amine equivalent of the paint is lower than a predetermined value.
  17. 제14항에 있어서,The method of claim 14,
    상기 품질은 pH를 포함하며,The quality comprises pH,
    상기 도료의 pH가 일정수치보다 낮아지도록 상기 도료를 상기 양이온수지에 통과시키는 단계를 포함하는 것을 특징으로 하는 전착도장 도료의 품질관리방법.Quality control method of the electrodeposition coating paint comprising the step of passing the paint through the cationic resin so that the pH of the paint is lower than a predetermined value.
PCT/KR2016/010760 2015-09-30 2016-09-26 System for managing quality of paint for electrodeposition, and method for managing quality of paint for electrodeposition using same WO2017057883A1 (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60200999A (en) * 1984-03-22 1985-10-11 Honny Chem Ind Co Ltd Method for regenerating mat paint for electrodeposition
KR0160485B1 (en) * 1995-06-15 1999-01-15 김광순 Color coating method on metal surface
JP2005336559A (en) * 2004-05-27 2005-12-08 Pi R & D Co Ltd Continuous electrodeposition coating apparatus
KR20060114711A (en) * 2003-12-31 2006-11-07 더 비오씨 그룹, 인크. Selective fluoride and ammonia removal by chromatographic separation of wastewater
KR20130103507A (en) * 2010-09-13 2013-09-23 오엠지 일렉트로닉 케미컬즈, 엘엘씨 Methods and apparatuses for treating a dispersion bath

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101286840B1 (en) 2006-07-20 2013-07-17 현대모비스 주식회사 Coating composition for plastic and eletro deposition coating of automobile

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60200999A (en) * 1984-03-22 1985-10-11 Honny Chem Ind Co Ltd Method for regenerating mat paint for electrodeposition
KR0160485B1 (en) * 1995-06-15 1999-01-15 김광순 Color coating method on metal surface
KR20060114711A (en) * 2003-12-31 2006-11-07 더 비오씨 그룹, 인크. Selective fluoride and ammonia removal by chromatographic separation of wastewater
JP2005336559A (en) * 2004-05-27 2005-12-08 Pi R & D Co Ltd Continuous electrodeposition coating apparatus
KR20130103507A (en) * 2010-09-13 2013-09-23 오엠지 일렉트로닉 케미컬즈, 엘엘씨 Methods and apparatuses for treating a dispersion bath

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