KR100270175B1 - Membrane separation - Google Patents
Membrane separation Download PDFInfo
- Publication number
- KR100270175B1 KR100270175B1 KR1019980010202A KR19980010202A KR100270175B1 KR 100270175 B1 KR100270175 B1 KR 100270175B1 KR 1019980010202 A KR1019980010202 A KR 1019980010202A KR 19980010202 A KR19980010202 A KR 19980010202A KR 100270175 B1 KR100270175 B1 KR 100270175B1
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- separator
- treated water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D65/00—Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
- B01D65/08—Prevention of membrane fouling or of concentration polarisation
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
- B01D61/10—Accessories; Auxiliary operations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
- B01D61/14—Ultrafiltration; Microfiltration
- B01D61/20—Accessories; Auxiliary operations
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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
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/20—By influencing the flow
- B01D2321/2066—Pulsated flow
- B01D2321/2075—Ultrasonic treatment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2321/00—Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
- B01D2321/22—Electrical effects
- B01D2321/223—Polarity reversal
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- Engineering & Computer Science (AREA)
- Water Supply & Treatment (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Nanotechnology (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
본 발명은 역삼투막, 나노막, 한외여과막, 초정밀 여과막 등의 막분리 기술을 이용하여 각종 산업용수의 제조, 용질의 분리, 회수 및 각종폐수 처리시에 오염물질에 의하여 농도 분극현상 및 눈막힘 현상을 방지하는 방법에 관한 것이다.The present invention utilizes membrane separation techniques such as reverse osmosis membranes, nano membranes, ultrafiltration membranes, ultra-precision filtration membranes, and the like to reduce concentration polarization and clogging due to contaminants during the production of various industrial waters, separation and recovery of solutes, and various wastewater treatments. It is about how to prevent.
막 분리기술은 박막에 액체를 가압처리하여 용액속에 용질을 분리, 정제, 농축 등을 행하는 단위조작이다.Membrane separation technology is a unit operation that pressurizes a liquid on a thin film to separate, purify, and concentrate solutes in a solution.
각종 폐수를 정화처리 함에는 생물학적, 화학적 처리가 필연적으로 동반하여 처리시설의 규모가 커지고 전문관리요원에 의하여 적절한 약품의 선정 그리고 투여 및 특별한 관리가 필요하고 슬랏치의 발생량이 많아지는 등 경제적, 시간적 손실과 부담이 과다한 실정이다.In order to purify various wastewater, economic and time loss such as biological and chemical treatment is inevitably accompanied by the increase in the size of treatment facilities, selection of appropriate chemicals and administration and special management by specialist management personnel, and the generation of slatch. Excessive burden on the situation.
막 분리기술은 이러한 폐수중에 유용한 성분이나 유해한 성분을 가장 확실하게 분리하는 기술이므로 분리물질을 재활용하거나 집중적인 처리가 가능하고 처리 되어진 방류수도 중수도로 재활용 할수 있는 잇점이 있어 최근에 각광을 받고 있다.Membrane separation technology is the most reliably separating the useful and harmful components in such waste water, so the separation material can be recycled or intensive treatment, and the treated effluent can be recycled to heavy water.
그러나 막분리기술은 막의 종류, 내압성, 내약품성 등 막의 선정도 중요하지만 최대의 난점은 용존되어 있는 용매의 용질, 혹은 알카리금속류 등 극초미립자의 고형물이 분리막에 부착하여 분리막이 오염 됨으로서 농도분극현상으로 인한 내압상승 및 투과수의 량이 감소하거나 전혀 막의 구실을 못하게 되어 막의 교체주기가 짧아 현실성이 희박하여 널리 이용을 못하고 있다.However, the membrane separation technology is important for the selection of membranes such as membrane type, pressure resistance, and chemical resistance, but the biggest difficulty is concentration polarization due to contamination of membranes with solid particles of ultra-fine particles such as dissolved solvents or alkali metals. Due to the increase in pressure and the amount of permeated water is reduced or the membrane is not at all, the replacement cycle of the membrane is short, so the practicality is not widely used.
이를 위하여 처리수속에 막오염방지 약품을 첨가하거나 사용후에 가성소다, 제3인소다, 구연산, 차아염소산소다, 인산, 염산 등으로 세척하여 사용하고 있는 실정이다.To this end, membrane fouling prevention chemicals are added to the treated water or used after washing with caustic soda, tertiary soda, citric acid, sodium hypochlorite, phosphoric acid and hydrochloric acid.
이러한 방법은 또다시 세척수의 처리 및 복잡하고 번거러운 관리가 요망되어 경제적 손실이 따른다.This method again requires treatment of the wash water and complicated and cumbersome management, resulting in economic losses.
위의 투과수량 감소는 수압에 의한 분리막 표면의 농도 분극화 현상 및 분리막의 표면오염(Membrane Fouling)에 기인한다.The decrease in the amount of permeation is caused by the concentration polarization of the membrane surface and the surface fouling of the membrane by hydraulic pressure.
막 오염의 원인으로는 물리·화학적 인자로 알카리토 금속류, 단백질, 염(Salt), 지방 등이 분리막 표면에 부착하기 때문이다.Membrane contamination is due to physical and chemical factors such as alkaline metals, proteins, salts and fats that adhere to the membrane surface.
본 발명은 위에 기술한바와 같은 문제점을 해결하기 위한 수단으로 분리막과 분리막 사이의 투과수 통로를 겸한 전도성의 플라스틱 그물망 혹은 금속망을 삽입하여 서로 대치되게 하고 그 망에 직류방식으로 전류밀도 0.1~80A/d㎡의 범위내에서 양전기(+)와 음전기(-)가 상호 작용하도록 극변환 방식으로 전기를 통하게 하고 더욱 효과를 높이기 위하여 처리수와 막에 초음파 진동을 주어 막의 오염은 물론 물질의 균등화를 이루어 양질의 투과수을 보다 많이 얻어 각종산업의 용수와 폐수의 정화처리의 효율을 극대화 시키는데 목적이 있다.The present invention is a means for solving the problems as described above by inserting a conductive plastic mesh or metal mesh serving as a permeate passage between the membrane and the membrane to replace each other and the current density 0.1 ~ 80A in the network by the DC method Electrostatic vibration is applied to the treated water and the membrane in order to make the positive and negative electrodes interact with each other within the range of / dm2 and to increase the effect. The purpose is to maximize the efficiency of water and wastewater purification in various industries by obtaining more high quality permeate.
제1도는 분리막셀 구조도.1 is a structure of a separator cell.
제2도는 분리막셀 2매 적층대치 배치도.FIG. 2 is a layout of two membrane cells stacked and replaced.
제3도는 분리막셀 평면도.3 is a plan view of a separator cell.
제4도는 초음파 진동판.4 is an ultrasonic diaphragm.
제5도는 분리막셀과 초음파 진동판 배치 복합도.5 is a composite diagram of the separator cell and the ultrasonic diaphragm.
제6도는 막분리 투과효율 비교표.6 is a membrane separation permeation efficiency comparison table.
〈도면의 주요부분에 대한 부호의 설명〉<Explanation of symbols for main parts of drawing>
1 : 분리막 2 : 전도성 플라스틱 망1: separator 2: conductive plastic net
3 : 투과수통로 4 : 폴리프로피렌 수지3: permeate channel 4: polypropylene resin
5 : 5"셀 압결 보드 구멍 6 : 처리수 통로5: 5 "cell squeezed board hole 6: treated water passage
7 : 초음파 진동판 8 : 초음파 진동자7: ultrasonic vibrating plate 8: ultrasonic vibrator
9 : 절연체9: insulator
이하 첨부된 도면에 의해 상세히 설명하면 다음과 같다.Hereinafter, described in detail by the accompanying drawings as follows.
도 1,2는 분리막셀의 구조 및 a분리막 b분리막 2매를 대치 적층한 것을 도시 한것으로 (1) 분리막과 (1')분리막 사이에 (2) 전도성 플라스틱 그물망 또는 금속망을 삽입하여 (3) 투과수 통로를 만들고 상기 망에 직류방식으로 전류밀도 0.1~80A/d㎡의 범위내에서 양전기(+)와 음전기(-)가 상호작용 하도록 극 변한 방식으로 전기를 흘리게 되면 a)분리막셀 b)분리막 사이의 처리수에는 전장이 형성되어 물속의 모든 물질이 음전기(-)쪽으로 전기영동하여 상호 호극으로 분리막에 이물질이 부착하지 못하도록 하며 전자의 빈번한 이동으로 막에 핀홀이 형성되어 투과수의 유통이 원활하게 한다.1 and 2 illustrate the structure of a separator cell and two stacked separators a and b, wherein a conductive plastic mesh or a metal mesh is inserted between the separator and the separator. When a permeate passage is made and electricity flows in the polarized manner so that positive and negative electrodes interact with each other within a range of current density of 0.1-80 A / dm 2 by direct current method a) Separation membrane cell b) An electric field is formed in the treated water between the membranes so that all substances in the water are electrophoresed toward the negative electrode (-) to prevent foreign substances from adhering to the membranes with the positive polarity. Make it smooth.
도 3은 a) b)분리막셀의 평면을 도시하였으모 (4)폴리프로피렌 수지층은 분리막셀과 분리막셀 사이에 처리수의 통로를 확보하고 분리막을 적층하는데에 기계적 강도와 하우징의 역할을 하며 (5)는 분리막판을 적층하여 압결하는 보드구멍이다.Figure 3 shows a) b) the plane of the separator cell (4) The polypropylene resin layer plays a role of mechanical strength and housing in securing the passage of treated water between the separator cell and the separator cell and stacking the separator. Denoted at 5 is a board hole for laminating and crushing a separator plate.
도 4는 초음파 발생 진동판으로서 내부식성의 (7)스테인레스 강판에 초음파 발생진동판으로서 내부식성의 (7)스테인레스 강판에 초음파 발생진동자을 내부에 부착되었으며 초음파는 분리막 사이의 처리수 및 분리막 표면의 전기 영동을 더욱 더 효과적으로 가속화 시키는 역활을 하면서 물질을 균등화 시켜 물질의 농도 분극화 현상을 파괴하는데 도움을 준다.Fig. 4 shows an ultrasonic wave generating vibrator attached to a corrosion resistant (7) stainless steel plate as an ultrasonic wave generating plate and an ultrasonic wave generating vibrator on a corrosion resistant (7) stainless steel plate as an ultrasonic wave generating plate. It helps to break down the concentration polarization of the material by equalizing the material, acting to accelerate it even more effectively.
도 5는 분리막셀과 초음파 진동판의 복합 배치도를 도시한 것으로 실시예를 상세히 설명하면 (10)처리수 펌프로 처리수를 5~60kg/㎠압으로 (11) 처리수 유입구로 보내어 지면 도 1의 분리막셀의 (5) 처리수 통로를 통하여 전기영동과 초음파 진동을 받으며 (12) 농축수 출구로 농축 또는 분리되어 나와서 재활용장치 또는 집중적 후처리 장치로 이송되고 분리막과 분리막 사이의 투과수는 (3) 투과통로로 흘러나와(13) 투과수 출구를 통하여 중수도로 재활용 되거나 방류시킨다.FIG. 5 illustrates a composite arrangement of the separator cell and the ultrasonic diaphragm. Referring to the embodiment in detail, (10) the treated water pump is sent to the treated water inlet at a pressure of 5 to 60 kg / cm 2. (5) receiving electrophoresis and ultrasonic vibration through the treated water passage of the separator cell (12) concentrated or separated at the outlet of the concentrated water and transported to a recycling or intensive post-treatment unit, and the permeate between the membrane and the separator (3 13) It flows out into the permeate passage (13) and is recycled or discharged into the heavy water through the permeate outlet.
도 6은 분리막에 폐수를 통과시켰을때 투과수의 량을 시간으로 표시한 비교표를 도시 하였다.FIG. 6 shows a comparison table indicating the amount of permeated water when the wastewater is passed through the separator in time.
이상에서 상술한바와 같이 분리막과 분리막 사이의 투과수 통로에 전도성의 플라스틱 그물망 또는 금속망을 삽입하고 여기에 직류 전압을 상호 호극으로 가하고 적층된 분리막 판에 초음파 진동을 가하는 방법으로 막분리 처리기술중 최대의 난점인 분리막의 오염과 물질농도 분극 현상을 해소하여 투과수량을 높이고 막의 교체 수명을 연장하므로서 각종 산업 용수의 처리 및 폐수의 정화처리를 획기적으로 개선하여 환경보전비 부담경감 및 설치면적이 최소화를 도모하여 자원의 재활용과 환경보전에 크에 기여 할 것이다.As described above, in the membrane separation treatment technique, a conductive plastic net or metal net is inserted into the permeate passageway between the separator and the separator, and a DC voltage is applied to each other and an ultrasonic vibration is applied to the laminated separator plate. Reducing the burden of environmental preservation costs and minimizing the installation area by drastically improving the treatment of various industrial waters and the purification of wastewater by eliminating pollution and material concentration polarization, which are the biggest difficulties, It will also contribute to the recycling of resources and the conservation of the environment.
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JPH08323164A (en) * | 1995-05-30 | 1996-12-10 | Kubota Corp | Clogging preventive device in membrane separation device |
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JPH08323164A (en) * | 1995-05-30 | 1996-12-10 | Kubota Corp | Clogging preventive device in membrane separation device |
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