KR200177170Y1 - Industrial water purification system using activated carbon fiber electrode and membranes - Google Patents

Industrial water purification system using activated carbon fiber electrode and membranes Download PDF

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KR200177170Y1
KR200177170Y1 KR2019990022645U KR19990022645U KR200177170Y1 KR 200177170 Y1 KR200177170 Y1 KR 200177170Y1 KR 2019990022645 U KR2019990022645 U KR 2019990022645U KR 19990022645 U KR19990022645 U KR 19990022645U KR 200177170 Y1 KR200177170 Y1 KR 200177170Y1
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South Korea
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activated carbon
carbon fiber
fiber electrode
desalination
membrane separation
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KR2019990022645U
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Korean (ko)
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박광규
윤석원
원도영
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한국전력공사
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    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water, or sewage
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis, ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/38Liquid-membrane separation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/46Treatment of water, waste water, or sewage by electrochemical methods
    • C02F1/4604Treatment of water, waste water, or sewage by electrochemical methods for desalination of seawater or brackish water

Abstract

본 고안은 막(membrane)과 활성탄소섬유 전극을 이용한 용수처리 장치에 관한 것으로 보다 상세하게는 막 또는 필터 등을 이용하여 부유물 및 유기물을 제거하며, 활성탄소섬유 전극을 이용하여 불순이온을 흡착시키고, 연속전기 탈이온 장치를 이용하여 활성탄소섬유 전극에서 제거하지 못한 미량 이온을 제거하는 공정으로 구성되어 용수 처리시 화공약품을 사용하지 않는 환경친화적 용수처리 장치에 관한 것이다.The present invention relates to a water treatment apparatus using a membrane and an activated carbon fiber electrode, and more specifically, to remove suspended matter and organic matter using a membrane or a filter, and to adsorb impurity ions using an activated carbon fiber electrode. The present invention relates to an environmentally friendly water treatment device, which is composed of a process of removing trace ions that cannot be removed from an activated carbon fiber electrode by using a continuous electric deionizer.
본 고안은 막분리 전처리장치를 이용하여 용존 고형물 및 유기물을 제거하며, 활성탄소섬유전극 탈염장치를 사용하여 수중 양이온 및 음이온 불순물을 제거하고, 연속탈이온 장치를 사용하여 활성탄소섬유전극 탈염장치에서 유출된 미량이온을 제거함으로써 수처리시 화공약품을 사용하지 않으므로 폐액이 발생되지 않는 공업용수 생산장치를 제공함을 목적으로 한다.The present invention removes dissolved solids and organics by using membrane separation pretreatment, removes cations and anion impurities in water using activated carbon fiber electrode desalination, and uses active deionization in activated carbon fiber electrode desalination It is an object of the present invention to provide an industrial water production device that does not generate waste liquids by removing chemicals that have been spilled and thus do not use chemicals in water treatment.

Description

활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치 {Industrial Water Purification System Using Activated Carbon Fiber Electrode and Membranes}Industrial Water Production System Using Activated Carbon Fiber Electrode Desalination and Membrane Separation {Industrial Water Purification System Using Activated Carbon Fiber Electrode and Membranes}
본 고안은 막(membrane)과 활성탄소섬유 전극을 이용한 용수처리 장치에 관한 것으로 보다 상세하게는 막 또는 필터 등을 이용하여 부유물 및 유기물을 제거하며, 활성탄소섬유 전극을 이용하여 불순이온을 흡착시키고, 연속전기 탈이온 장치를 이용하여 활성탄소섬유 전극에서 제거하지 못한 미량 이온을 제거하는 공정으로 구성되어 용수 처리시 화공약품을 사용하지 않는 환경친화적 용수처리 장치에 관한 것이다.The present invention relates to a water treatment apparatus using a membrane and an activated carbon fiber electrode, and more specifically, to remove suspended matter and organic matter using a membrane or a filter, and to adsorb impurity ions using an activated carbon fiber electrode. The present invention relates to an environmentally friendly water treatment device, which is composed of a process of removing trace ions that cannot be removed from an activated carbon fiber electrode by using a continuous electric deionizer.
종래의 공업용수 생산장치는 응집과 침전을 위주로 한 전처리장치와 수중의 이온을 제거하기 위한 이온교환수지장치 및 처리수의 순도를 높이는 혼합이온교환수지 장치로 구성되어 있다. 그러나 산업발전에 따라 환경오염이 심해지고 원수의 수질이 악화됨에 따라 각 장치별 화공약품 소모량이 크게 증가할 뿐 아니라 폐수규제치가 강화됨에 따라 생산비용이 크게 증가하고, 경우에 따라서는 공업용수를 원활히 생산할 수 없는 실정이다.The conventional industrial water production apparatus is composed of a pretreatment apparatus mainly for flocculation and sedimentation, an ion exchange resin apparatus for removing ions from water, and a mixed ion exchange resin apparatus for increasing the purity of the treated water. However, as industrial development increases, environmental pollution and raw water quality deteriorate, the consumption of chemicals by each device not only increases greatly, but the production cost increases greatly as the regulation of wastewater increases, and in some cases, the industrial water is smoothly It cannot be produced.
응집침전 장치의 경우 운전 정지후 재 가동시 원수의 수질에 따라 정확한 운전 조건을 설정해 주지 않을 경우 원활한 침전이 이루어지지 않아 장치의 가동이 불가능해 지며, 이때 침전을 위하여 응집제, 응집보조제, 염산, 가성소다 등 다수의 화공약품을 사용하게 된다. 여기에 수중의 부유입자를 제거하기 위한 중력식 여과기가 추가로 필요하여 장치의 대형화 및 조작시 고도의 전문성이 요구되는 단점이 있다.In the case of flocculation sedimentation device, if the operation conditions are not set correctly according to the quality of raw water when restarting after the operation is stopped, the device is impossible to operate due to the smooth sedimentation. At this time, flocculant, flocculent aid, hydrochloric acid, caustic Many chemicals, including soda, will be used. In addition, a gravity filter for removing suspended particles in the water is additionally required, which requires a high degree of expertise in the enlargement and operation of the device.
또한, 응집침전 장치로 제거되지 않은 유기물 등의 제거를 위하여 활성탄이 포함된 충진탑을 사용하여야 하고, 각종 이온성분을 제거하기 위하여 이온교환수지탑을 사용하여야 하는데 이 역시 대형의 장치가 필요하고 운전시 전문성 및 지속적인 주의를 필요로 하며, 재생시 화공약품을 사용하여 다량의 재생폐액이 발생되는 단점이 있다.In addition, a packing tower containing activated carbon should be used to remove organic matters not removed by the flocculation settling device, and an ion exchange resin tower should be used to remove various ionic components. It requires expertise and continuous attention, and has a disadvantage in that a large amount of recycled waste is generated by using chemicals during regeneration.
본 고안은 종래의 수처리상의 단점을 해결하기 위하여 막분리 전처리장치를 이용하여 용존 고형물 및 유기물을 제거하며, 활성탄소섬유전극 탈염장치를 사용하여 수중 양이온 및 음이온 불순물을 제거하고, 연속탈이온 장치를 사용하여 활성탄소섬유전극 탈염장치에서 유출된 미량이온을 제거함으로써 수처리시 화공약품을 사용하지 않으므로 폐액이 발생되지 않는 공업용수 생산장치를 제공함을 목적으로 한다.The present invention removes dissolved solids and organics using membrane separation pretreatment device to solve the disadvantages of conventional water treatment, removes cations and anion impurities in water using activated carbon fiber electrode desalination device, and continuously deionization device. It is an object of the present invention to provide an industrial water production apparatus that does not use waste chemicals during water treatment by removing the trace temperature leaked from the activated carbon fiber electrode desalination apparatus.
도 1은 공업용수 생산공정의 개략도1 is a schematic diagram of an industrial water production process
도 2a는 직렬운전용 평판형 활성탄소섬유전극 탈염장치의 내부상세도Figure 2a is a detailed internal view of the flat activated carbon fiber electrode desalination apparatus for series operation
도 2b는 병렬운전용 평판형 활성탄소섬유전극 탈염장치의 내부상세도Figure 2b is a detailed internal view of the planar activated carbon fiber electrode desalination apparatus for parallel operation
도 2c는 직렬,병렬 혼용운전용 평판형 활성탄소섬유전극 탈염장치의 내부상세도Figure 2c is a detailed internal view of the flat activated carbon fiber electrode desalination apparatus for serial, parallel mixed operation
도 2d는 평판형 활성탄소섬유전극 탈염장치의 내부상세도Figure 2d is a detailed internal view of the plate-type activated carbon fiber electrode desalination apparatus
도 3은 나권형 활성탄소섬유전극 탈염장치의 내부상세도Figure 3 is a detailed internal view of the spiral wound activated carbon fiber electrode desalination apparatus
<도면의 주요부분에 대한 부호의 설명><Explanation of symbols for main parts of the drawings>
10: 막분리 전처리장치 20: 활성탄소섬유 탈염장치10: membrane separation pretreatment device 20: activated carbon fiber desalination device
21: 양극의 활성탄소섬유판 22: 음극의 활성탄소섬유판21: activated carbon fiber plate of positive electrode 22: activated carbon fiber plate of negative electrode
23: 유로형성판 24: 실리콘판 25: + 전극23: flow path forming plate 24: silicon plate 25: + electrode
26: 활성탄소섬유판 27: 나일론 망사 28: -전극26: activated carbon fiber plate 27: nylon mesh 28:-electrode
29: 활성탄소섬유판 30: 분리판 31: 처리수입구29: activated carbon fiber plate 30: separation plate 31: treatment inlet
32: 처리수 출구 33: 상부뚜껑 34: 하부뚜껑32: treated water outlet 33: upper lid 34: lower lid
40: 나권형 활성탄소섬유장치 41', 41': 분리판40: spiral wound activated carbon fiber device 41 ', 41': separator
42: ACF양극 43: ACF음극 44: 몸체42: ACF anode 43: ACF cathode 44: body
45: 투입구 45': 상부 뚜껑 46: 배출구45: inlet 45 ': upper lid 46: outlet
46': 하부 뚜껑46 ': lower lid
본 고안의 장치는 막분리 전처리장치(10), 활성탄소섬유전극 탈염장치(20), 연속전기탈이온 장치(40)로 구성되어 있으며 종래의 응집침전조, 중력식여과기, 활성탄탑을 대신할 수 있는 장치로서 막분리 전처리 장치(10)는 중공사 형태의 막을 이용하여 부유물 및 유기물을 제거하며 역세를 통해 별도의 화공약품 사용 없이 세정 및 운전이 가능한 한국정수(주)의 프리필 또는 폴리에스텔 섬유를 열융착 가공한 CHIP을 일정한 밀도로 배열하여 세척을 쉽게 할 수 있는 마이크로 칩 필터(JONG HAB POLLUTION Co.의 제품)를 적용하였다.The device of the present invention is composed of membrane separation pretreatment device (10), activated carbon fiber electrode desalination device (20), continuous electric deionization device (40), and can replace the conventional coagulation sedimentation tank, gravity filter, activated carbon tower. As a device, the membrane separation pretreatment device 10 removes suspended matter and organic matter by using hollow fiber membranes and heats prefilled or polyester fibers of Korea Water Purification Co., Ltd., which can be cleaned and operated without the use of chemicals. A microchip filter (product of JONG HAB POLLUTION Co.), which can be easily cleaned by arranging the melted chip at a constant density, was applied.
막분리 전처리장치의 후단에는 종래의 이온교환수지탑 탈염기를 대신한 장치로 활성탄소섬유전극 방식의 탈염장치(20)를 사용하였고, 활성탄소섬유 탈염장치 후단에는 종래의 혼상수지탑을 대신한 장치로서 이온교환수지, 이온교환막 및 전극을 이용하여 이온교환수지를 전기적으로 재생하는 한국정수(주)의 MDI를 연속탈이온 장치(40)로 사용하여 활성탄소섬유 탈염장치에서 유출된 미량이온을 제거하여 처리수의 순도를 높일 수 있도록 하였다.The rear end of the membrane separation pretreatment device used an activated carbon fiber electrode desalination device (20) as a device replacing the conventional ion exchange resin tower desalter, and the rear end of the activated carbon fiber desalting device (a device replacing the conventional mixed bed resin tower). As a continuous deionizer (40), MDI of Korea Co., Ltd., which regenerates the ion exchange resin electrically by using an ion exchange resin, an ion exchange membrane and an electrode, removes trace ions from the activated carbon fiber desalination unit. To increase the purity of the treated water.
도 2a, 2b, 2c은 도 2d에서와 같이 두께 3mm의 실리콘 판(24) 안에 내부크기와 같은 형태의 활성탄소 섬유판(26)(일본 KURACTIVE사의 활성탄소섬유)을 넣고 실리콘 판(24)의 내부를 통과한 (+)전극(25)을 활성탄소 섬유판(26)에 연결하여 양극의 활성탄소 섬유판(21)을 형성한다. 양극의 활성탄소섬유판과 포개어지는 유로형성판(23)은 두께 5mm의 엔지니어링 플라스틱 판(26)(ABS/PC)안에 두께 5mm의 나일론 망사(27)로 유로를 형성하며 동시에 양극과 음극의 활성탄소 섬유판이 접촉하지 않게 방지하고, 위와 아래에 내경 3mm의 처리수 입구(31)와 출구(32)가 존재한다. 유로형성판(23)과 포개어지는 음극의 활성탄소 섬유판(22)은 두께 3mm의 실리콘 판(24) 안에 내부크기와 같은 형태의 활성탄소 섬유판(29)을 넣고 실리콘판 (24)의 내부를 통과한 (-)전극(28)을 활성탄소 섬유판(29)과 연결하여 음극의 활성탄소 섬유판(22)을 형성한다. 음극의 활성탄소 섬유판(22)과 포개어지는 분리판(30)은 두께 2mm의 엔지니어링 플라스틱으로, 양극의 활성탄소섬유판(21), 유로형성판(23), 음극의 활성탄소 섬유판(22)이 이루는 유로를 다른층과 분리하여 적층하기 위한 역할을 한다. 이때 모듈은 양극의 활성탄소 섬유판(21)에서 분리판(30) 까지가 예를 들어 10층 이상 적층되며, 양 끝에 상부뚜껑(33)과 하부뚜껑(34)을 두고 볼트구멍 (35)을 통해 볼트(SUS304)로 조여 하나의 모듈을 구성한다.2A, 2B and 2C show the inside of the silicon plate 24 with the activated carbon fiber plate 26 (active carbon fiber manufactured by KURACTIVE, Japan) of the same size as the inside of the silicon plate 24 having a thickness of 3 mm as shown in FIG. 2D. The positive electrode 25 passed through is connected to the activated carbon fiber plate 26 to form the activated carbon fiber plate 21 of the positive electrode. The active carbon fiber plate of the positive electrode and the flow path forming plate 23 are formed of a nylon mesh 27 of 5 mm thick in an engineering plastic plate 26 (ABS / PC) having a thickness of 5 mm, and at the same time, the activated carbon of the positive electrode and the negative electrode To prevent the fiberboard from contacting, there is a treated water inlet 31 and outlet 32 having an inner diameter of 3mm above and below. The activated carbon fiber plate 22 of the negative electrode overlapped with the flow path forming plate 23 is placed in the silicon plate 24 having a thickness of 3 mm by inserting the activated carbon fiber plate 29 having the same shape as the inside size and passing through the inside of the silicon plate 24. One negative electrode 28 is connected to the activated carbon fiber plate 29 to form an activated carbon fiber plate 22 of the negative electrode. The separator 30 overlapping the activated carbon fiber plate 22 of the negative electrode is an engineering plastic having a thickness of 2 mm, and is formed of the activated carbon fiber plate 21 of the positive electrode, the flow path forming plate 23, and the activated carbon fiber plate 22 of the negative electrode. It serves to stack the flow path separately from other layers. At this time, the module is stacked, for example, more than 10 layers from the activated carbon fiber plate 21 of the positive electrode to the separator 30, through the bolt hole 35 with the upper lid 33 and the lower lid 34 at both ends. Tighten with bolt SUS304 to form one module.
막분리 전처리장치(10)를 거쳐 나온 물을 이 활성탄소섬유판 사이에 형성된 유로(27)로 용수를 흐르게 하고, 전류를 흘려 양극의 활성탄소섬유판(21)에는 음이온불순물이 전기적으로 부착되고, 음극의 활성탄소섬유판(22)에는 양이온불순물이 전기적으로 부착되도록 구성되어 있다. 이와 같이 부착된 양이온 및 음이온 불순물은 활성탄소섬유판에 전기를 통하지 않을 경우 활성탄소섬유판에서 떨어져 나오게 되므로 별도의 화공약품을 사용하지 않고 활성탄소섬유판의 세척이 가능해진다.Water flowing through the membrane separation pretreatment device 10 is flowed into the flow path 27 formed between the activated carbon fiber plates, and an anion impurity is electrically attached to the activated carbon fiber plate 21 of the positive electrode by flowing a current. The activated carbon fiber plate 22 is configured to be electrically attached to the cation impurities. The cation and anion impurities attached as described above are separated from the activated carbon fiber plate when the activated carbon fiber plate is not electricity, and thus the activated carbon fiber plate can be washed without using a separate chemical agent.
이와 같은 활성탄소섬유판이 여러층, 예를 들어 10층 이상 적층하여 하나의 모듈을 구성하게 된다.Such activated carbon fiber plate is laminated in several layers, for example, ten or more layers to form one module.
또한, 처리수의 순도를 높이고자 할 경우 활성탄소섬유판을 직렬로 연결하여 유로를 형성(도 2a)하고, 생산수의 양을 많게 하기 위해서는 병렬로 연결(도 2b)할 수 있게 하여 운전상황에 따른 대처가 용이하게 하였다. 또한, 폐액의 규제 기준치에 따라 활성탄소 섬유판을 직렬 또는 병렬을 혼합 사용(도 2c)할 수 있게 하였다.In addition, in order to increase the purity of the treated water, the activated carbon fiber boards are connected in series to form a flow path (FIG. 2A), and in order to increase the amount of water produced, it is possible to connect in parallel (FIG. 2B) to the operating situation. Easy to cope with. In addition, the activated carbon fiberboard can be used in series or in parallel (FIG. 2C) in accordance with the regulation of waste liquid.
도 3은 다공성 망(분리판)의 절연체를 사용하여 (+)극과 (-)극의 활성탄소섬유를 절연시킨 후 분리판(41'), (+)극 활성탄소섬유(42), 절연시킨 분리판(41'), (-)극 활성탄소섬유(43)를 포개어 나권형으로 말아 모듈(도 3)을 형성하여 원통 (44)안에 넣고 상부 뚜껑(45')과 하부 뚜껑(46')을 한 후 투입구(45)와 배출구(46)를 부착한다. 이 때 모듈의 배열 방식은 용수의 수질과 수량, 폐수의 성상 조절이 용이하도록 직렬 또는 병렬로 조합할 수 있으며, 모듈을 나권형 또는 평판형으로 구성할 수 있다.3 is used to insulate the activated carbon fibers of the (+) and (-) poles using an insulator of a porous net (separator plate), then the separator (41 '), (+) pole activated carbon fibers (42), insulation The separator (41 ') and (-) pole activated carbon fibers (43) stacked and rolled into a spiral wound to form a module (FIG. 3), and placed in the cylinder 44. The upper lid 45' and the lower lid 46 ' ) And then attach the inlet (45) and outlet (46). At this time, the arrangement of the modules can be combined in series or in parallel to easily control the water quality and quantity of the water, and the properties of the wastewater, the module can be configured in a spiral wound or flat plate type.
평판형 활성탄소섬유 탈염장치(20)을 거쳐 탈염된 물이 투입구(45)를 통하여 물을 공급하면 활성탄소섬유의 내부면을 통과하면서 (+)극의 활성탄소섬유를 통과하면서 음이온이 활성탄소섬유에 흡착되고, (-)극의 활성탄소섬유를 통과하면서 양이온이 활성탄소에 흡착되어 처리수의 순도를 높이게 된다. 이와 같은 모듈을 복수의 직렬 또는 병렬로 연결하면 원하는 고순도의 수질을 얻을 수 있다.When the desalted water is supplied through the inlet 45 through the flat activated carbon fiber desalination apparatus 20, the anion is activated carbon while passing through the inner surface of the activated carbon fiber and passing through the activated carbon fiber of the positive electrode. Adsorbed to the fibers, the positive ions are adsorbed to the activated carbon while passing through the activated carbon fibers of the (-) pole to increase the purity of the treated water. By connecting such modules in series or in parallel, the desired high purity water quality can be achieved.
<시험예><Test Example>
본 고안의 장치를 이용하여 단계별로 제조한 물의 순도를 표 1에 나타냈다.Table 1 shows the purity of the water produced step by step using the device of the present invention.
표 1. 본 고안의 장치를 이용하여 제조한 물의 순도Table 1. Purity of water produced using the device of the present invention
구 분division 막분리 전처리장치Membrane Separator 활성탄소섬유탈염장치Activated Carbon Fiber Desalination Equipment 연속 탈이온 장치Continuous deionizer
유입수 수질(μS/cm)Influent Water Quality (μS / cm) 150150 120120 1010
처리수 수질(μS/cm)Treated water quality (μS / cm) 120120 1010 0.10.1
본 고안은 용수의 처리시 화공약품을 사용하지 않으므로 폐액이 발생되지 않는 환경 친화적 공정이고, 활성탄소전극판을 재생시 별도의 약품이나 전력사용 없이 전원만 차단하면 재생됨에 따라 별도의 에너지 소모 없이 재생할 수 있어 운영경비가 저렴하다.The present invention is an environmentally friendly process that does not generate waste liquids because it does not use chemicals in the treatment of water, and it can be regenerated without extra energy consumption by regenerating the activated carbon electrode plate when the power is cut off without the use of chemicals or power. Operation cost is low.
또한 막과 전극을 이용한 이온흡착 방식의 채택으로 기존의 처리장치에 비해 작동이 손쉽고 장치의 소요면적이 상대적으로 적으며 자동운전이 가능할 뿐만 아니라 처리수의 수질과 수량 및 폐액 성상을 용이하게 조절할 수 있다.In addition, by adopting the ion adsorption method using membrane and electrode, it is easier to operate than the existing treatment device, the area of the device is relatively small, and automatic operation is possible, and it is possible to easily control the water quality, quantity and waste liquid properties of treated water. have.

Claims (5)

  1. 비화학적인 용수 처리장치에 있어서, 막분리 전처리장치(10)와 활성탄소섬유전극 탈염장치(20) 및 연속탈이온장치(40)를 조합하여 일련의 물처리 장치로 구성하는 것을 특징으로 하는 활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치.In the non-chemical water treatment apparatus, the membrane separation pretreatment apparatus 10, the activated carbon fiber electrode desalination apparatus 20, and the continuous deionization apparatus 40 are combined to form a series of water treatment apparatuses. Industrial water production equipment using carbon fiber electrode desalination and membrane separation.
  2. 제 1항에 있어서, 활성탄소섬유전극 탈염장치(20)는 (+)극 활성탄소섬유판과 (-)극 활성탄소섬유판으로 구성된 모듈을 하나 이상으로 형성시켜 직렬, 병렬, 또는 직렬 병렬을 혼합하여 사용할 수 있도록 구성되는 것을 특징으로 하는 활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치The method of claim 1, wherein the activated carbon fiber electrode desalination apparatus 20 is formed by forming one or more modules consisting of a (+) pole activated carbon fiber plate and a (−) pole activated carbon fiber plate by mixing in series, parallel, or series parallel Industrial water production apparatus using the activated carbon fiber electrode desalination method and membrane separation method characterized in that configured to be used
  3. 제 1항에 있어서, 탈이온 장치는 절연체로 (+)극 활성탄소섬유(42)와 (-)극활성탄소섬유(43)를 절연시킨 후 분리판(41')과 (41')로 (-)극 활성탄소섬유와 (+)극 활성탄소섬유에 포개어 나권형으로 말아 모듈을 형성시켜 원통(44)안에 넣고 상부 뚜껑(45')과 하부 뚜껑(46')을 하여 투입구(45)와 배출구(46)를 부착시켜 구성된 것을 특징으로 하는 활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치.The deionizer according to claim 1, wherein the deionization device insulates the (+) polar activated carbon fibers 42 and (-) polar activated carbon fibers 43 with an insulator, and then divides them into separators 41 'and (41'). -) Formed into a spiral wound type by superimposing on the activated carbon fiber and the (+) polar activated carbon fiber, and putting it in the cylinder (44). Industrial water production apparatus using the activated carbon fiber electrode desalination method and membrane separation method characterized in that the outlet 46 is attached.
  4. 제 3항에 있어서, 활성탄소 전극의 모듈 배열 방식을 직렬 또는 병렬로 조합하는 것을 특징으로 하는 활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치.The apparatus for producing industrial water using an activated carbon fiber electrode desalination method and a membrane separation method according to claim 3, wherein the module arrangement of activated carbon electrodes is combined in series or in parallel.
  5. 제 3항에 있어서, 활성탄소 모듈을 나권형 또는 평판형으로 구성하는 것을 특징으로 하는 활성탄소섬유전극 탈염법과 막분리법을 이용한 공업용수 생산장치.4. The apparatus for producing industrial water using an activated carbon fiber electrode desalting method and a membrane separation method according to claim 3, wherein the activated carbon module is configured in a spiral wound or flat plate type.
KR2019990022645U 1999-10-20 1999-10-20 Industrial water purification system using activated carbon fiber electrode and membranes KR200177170Y1 (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100420314B1 (en) * 2000-08-31 2004-03-04 (주)바이오준테크 The Wastewater Treatment Method and its System
KR100433132B1 (en) * 2002-02-28 2004-05-27 한국정수공업 주식회사 Desalinization device using porosity carbon electrode and porosity insulator
KR100445575B1 (en) * 2002-06-20 2004-08-25 한국전력공사 Device for removing the inorganic materials and ion of elecdtrode cell
KR100762008B1 (en) * 2006-05-29 2007-10-04 (주)경인양행 Water-treatment system of improved recovery rate

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100420314B1 (en) * 2000-08-31 2004-03-04 (주)바이오준테크 The Wastewater Treatment Method and its System
KR100433132B1 (en) * 2002-02-28 2004-05-27 한국정수공업 주식회사 Desalinization device using porosity carbon electrode and porosity insulator
KR100445575B1 (en) * 2002-06-20 2004-08-25 한국전력공사 Device for removing the inorganic materials and ion of elecdtrode cell
KR100762008B1 (en) * 2006-05-29 2007-10-04 (주)경인양행 Water-treatment system of improved recovery rate

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