KR20040092663A - Apparatus for electro-coagulative treatment with conductive media - Google Patents

Apparatus for electro-coagulative treatment with conductive media Download PDF

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Publication number
KR20040092663A
KR20040092663A KR1020030026171A KR20030026171A KR20040092663A KR 20040092663 A KR20040092663 A KR 20040092663A KR 1020030026171 A KR1020030026171 A KR 1020030026171A KR 20030026171 A KR20030026171 A KR 20030026171A KR 20040092663 A KR20040092663 A KR 20040092663A
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South Korea
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housing
electrode
coagulant
wastewater
media
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KR1020030026171A
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Korean (ko)
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권인자
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권인자
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    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/463Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrocoagulation
    • 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
    • C02F1/461Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
    • C02F1/46104Devices therefor; Their operating or servicing
    • C02F1/46109Electrodes
    • C02F2001/46119Cleaning the electrodes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2303/00Specific treatment goals
    • C02F2303/22Eliminating or preventing deposits, scale removal, scale prevention

Abstract

PURPOSE: Provided is an electro-coagulating apparatus by using conductive media which is able to continuously allow wastewater to flow in and electrically coagulate the wastewater to treat it. CONSTITUTION: The apparatus comprises a housing (10) having a watching window (11) and an electrode plate (51), a storage case (40) where cohesive agents eluting metals (70) such as expendable aluminum or iron are stored, conductive media (60) filled up with the inner space of the lower part of the housing, an electrode rod (50) equipped at the center of the storage case and fixed on an upper cover (20), the upper cover (20) having an outlet (21) connected to an inlet of cohesive agents eluting metals (22), a lid (23) and an upper part strainer (24) and connected by a bolt and nut (25) to the housing, and a lower part cover (30) having an inlet (31) connected to the lower part strainer (32) and connected by a bolt and nut (33) to the housing.

Description

전도성 메디아를 이용한 전기응집처리 장치 {Apparatus for electro-coagulative treatment with conductive media }Apparatus for electro-coagulative treatment with conductive media

본 발명은 절연성 원통체로 구성된 하우징(10) 하부커버(30)의 유입구(31)을 통해 유입되는 폐수의 통과 유속에 의해 전도성메디아(60)를 상부로 이동시킴으로 전류효율의 극대화와 전도성메디아(60)의 전극판(51)표면 마찰을 통해 하우징(10)내의 전극에 스케일 형성을 방지할 수 있으며, 아울러 전기분해에 의해 산화성물질을 발생시켜 물속의 오염물질을 산화시키고, 응집제용출금속(70)으로부터 용출된 금속이온에 의한 전기응집작용으로 화학반응을 일으켜서 부유물과 콜로이드 입자를 응집시킴으로써 오염물질 제거가 용이해지는 전도성 메디아를 이용한 전기응집처리장치에 관한 것이다.The present invention maximizes the current efficiency and the conductive media (60) by moving the conductive media (60) to the upper by the flow rate of the wastewater flowing through the inlet 31 of the lower cover 30 of the housing 10 consisting of an insulating cylindrical body The surface friction of the electrode plate 51 can prevent the formation of scale on the electrode in the housing 10, and also generate an oxidizing substance by electrolysis to oxidize contaminants in the water, and the coagulant eluting metal (70) The present invention relates to an electroaggregation treatment apparatus using a conductive medium, which causes a chemical reaction by coagulation by metal ions eluted from the coagulation of floc and colloidal particles, thereby facilitating removal of contaminants.

일반적으로, 각종 산업폐수 및 생활오수 처리방법으로는 침전 ,여과 등을 이용한 물리적 처리방법, 화학약품을 투입하여 화학 반응에 의한 처리를 하는 화학적 처리방법, 미생물을 이용하여 유기물을 분해 처리하는 생물학적 처리방법이 주종을 이루고 있다.In general, various industrial wastewater and sewage treatment methods include physical treatment using sedimentation and filtration, chemical treatment using chemical reactions by adding chemicals, and biological treatment using organic microorganisms to decompose organic matters. The method prevails.

이와 같은 종래의 폐수처리장치는 설치규모가 크고, 설치 구조가 복잡하여 설치비용이 고가일 뿐만 아니라 설치규모의 크기로 인하여 대규모의 설치면적이 필요하며, 설치한 경우에도 설치구조가 복잡하여 고도의 처리기술이 필요하고, 이로 인한 운전 미숙 및 전문성의 결여로 인하여 처리장치를 정상적으로 가동할 수 없는 문제점이 있었다.Such a conventional wastewater treatment apparatus has a large installation scale, a complicated installation structure, and a high installation cost, and a large installation area is required due to the size of the installation scale. There is a problem in that the processing technology is required, and thus, the processing apparatus cannot be normally operated due to immature operation and lack of expertise.

이러한 점들을 감안하여 보다 용이하게 폐수처리장치를 운전할 수 있도록 한 전기분해를 이용한 전기응집처리 방법이 사용되고 있다.In view of these points, an electroaggregation treatment method using electrolysis, which makes it easier to operate the wastewater treatment apparatus, has been used.

이와 같은 전기응집처리 방법은 폐수를 저장하는 저장조에 다수의 음극과 양극의 전극판을 침전시켜 이의 전극판에서 발생되는 양,음이온과 폐수와의 전기반응으로 인해 폐수를 처리하는 것으로 유분, 무기성 오염물질, 유기성오염물질 및 콜로이드성 오염물질 제거에 효과적이며, 장치의 크기에 비하여 고농도의 오염폐수를 처리할 수 있는 장점이 있다.Such an electrocoagulation treatment method is to treat the waste water due to the electrical reaction between the positive and negative ions generated in the electrode plate by depositing the electrode plates of the plurality of cathodes and anodes in the storage tank for storing the waste water. Effective in removing contaminants, organic contaminants and colloidal contaminants, and has the advantage of treating high concentrations of contaminated wastewater compared to the size of the device.

그러나, 이러한 전기응집처리 방법은 일정시간이 경과하게 되면 양극 전극이 소모되어 전극을 교체해야하며, 전극교체시 운전 중단 및 교체전극의 폐기물 처리 문제등 어려운점이 많으며, 스케일의 형성을 방지하거나 전극의 수명 연장을 위하여 주기적으로 역전을 거는 방법을 사용하고 있지만 ,운전시간 경과에 따른 전극판에 스케일이나 스컴과 같은 찌꺼기가 전극판에 부착 되어 처리효율을 감소시키는 문제가 있었다.However, this method of electroaggregation requires the replacement of the electrode after a certain amount of time is exhausted, and there are many difficulties such as interruption of operation and waste disposal of the replacement electrode. In order to extend the service life, a method of periodically reversing is used, but there is a problem in that processing efficiency decreases due to adhesion of scale or scum to the electrode plate over the operation time.

또한 ,대부분의 전기응집처리 장치는 유입되는 폐수내의 염성분이 낮은 경우 전기효율이 낮아 전기분해가 원활하게 일어나지 않기 때문에 전해질을 주입하는 경우도 있으며, 장치가 밀봉된 가압형이 아닌 일정부분이 개방된 형태로 ,전극 부분이 노출되어 운전시 안전사고를 유발할 수 있는 단점이 있었다.In addition, most electro-agglomerate treatment devices are injected with electrolyte because the electrolysis is low when the salt content in the influent wastewater is low and the electrolysis does not occur smoothly. In the form, there was a disadvantage that the electrode portion is exposed can cause a safety accident during operation.

따라서 본 발명은 상기의 제반 문제점을 해결하기 위하여 안출 된 것으로서, 절연성 원통체로 구성된 하우징(10)의 하부커버(30)에 구비된 유입구(31)을 통해 유입되는 폐수의 통과 유속에 의해 전도성메디아(60)를 상부로 이동시킴으로 염성분이 적은 폐수나 용수에서도 전기가 잘 흐르게 하여 전류효율을 높이고 전도성메디아(60)에의한 전극표면 마찰을 통해 하우징(10)내의 전극판(51)에 스케일이나 찌꺼기의 부착을 방지할 수 있으며, 아울러 전기분해에 의해 산화성물질을 발생시켜 폐수 속의 오염물질을 산화시키고, 응집제용출금속(70)으로부터 용출된 금속이온에 의한 전기응집 작용으로 화학반응을 일으켜서 부유물과 콜로이드 입자를 응집시킴으로써 오염물질 제거가 용이해지며, 응집제용출금속(70)이 소모되면 손쉽게 보충할 수 있도록 하였으며, 밀폐된 내부에 전극이 위치하여 운전시 전극에 의한 위험을 방지하며, 가압형으로 연속적으로 폐수를 처리할 수 있도록 한 전도성 메디아를 이용한 전기응집처리 장치를 제공함에 그 목적이 있다.Therefore, the present invention has been made in order to solve the above problems, the conductive media by the flow rate of the waste water flowing through the inlet 31 provided in the lower cover 30 of the housing 10 composed of an insulating cylindrical body ( 60) is moved upwards, so that electricity flows well in waste water or water with low salt content, and improves current efficiency, and through the surface friction by the conductive media 60, Adhesion can be prevented, and oxidative substances are generated by electrolysis to oxidize contaminants in the wastewater, and chemical reactions are caused by electrocoagulation by metal ions eluted from the coagulant-eluting metal (70). It is easy to remove the contaminants by agglutinating, and when the coagulant eluting metal 70 is consumed, it can be easily replenished. It is an object of the present invention to provide an electrocoagulation treatment apparatus using a conductive media that can be disposed in a sealed interior to prevent the danger caused by the electrode during operation and to continuously treat the wastewater in a pressurized manner.

도 1은 본 발명에 의한 전기응집처리장치 단면도1 is a cross-sectional view of the electroaggregation apparatus according to the present invention

도 2는 본 발명의 일 실시예의 작동 상태도2 is an operating state diagram of an embodiment of the present invention

*도면의 주요부분에 대한 부호의 설명** Description of the symbols for the main parts of the drawings *

10 : 하우징 11: 감시창10 housing 11: monitoring window

20 : 상부커버 21: 배출구20: top cover 21: outlet

22 : 투입구 23 : 뚜껑22: inlet 23: lid

24 : 상부스트레이너 25,33: 볼트,너트24: Upper strainer 25, 33: Bolt, nut

30: 하부커버 31 : 유입구30: lower cover 31: inlet

32 : 하부스트레이너 40 : 저장통32: lower strainer 40: reservoir

50 : 전극봉 51 : 전극판50: electrode 51: electrode plate

52 : 음극단자 53 : 양극단자52: cathode terminal 53: anode terminal

60 : 전도성메디아 70 : 응집제용출금속60: conductive media 70: flocculant eluting metal

상기 목적을 달성하기 위하여 본 발명에서는 절연성 원통체로 구성된 하우징(10) 상부 외측 벽면에 감시창(11)과 내측 벽면에 전극판(51)이 위치하고, 그 내부에 소모성 알루미늄이나 철과 같은 응집제용출금속(70)이 저장되는 저장통(40)이 구비되며, 하우징(10) 아래쪽 내부 공간에는 전도성메디아(60)가 충진되고, 저장통(40) 중간에 양극으로 인가되는 전극봉(50)은 상부 커버(20)에 고정되며, 응집제용출금속(70) 투입구(22)와 뚜껑(23)과 상부스트레이너(24)와 연결되는 배출구(21)을 포함하는 상부커버(20)는 하우징(10)과 볼트너트(25)로 고정되며, 하부스트레이너(32)와 연결되는 유입구(31)가 구비된 하부커버(30)는 볼트너트(33)로 하우징(10)과 연결되어 폐수를 연속적으로 유입시켜 전기적으로 응집 처리할 수 있도록 구성함을 특징으로 하여 달성된다.In order to achieve the above object, in the present invention, the monitoring window 11 and the electrode plate 51 are positioned on the inner wall of the housing 10 and the outer wall of the housing 10 composed of an insulating cylindrical body. A storage container 40 in which the 70 is stored is provided, and the conductive medium 60 is filled in the inner space below the housing 10, and the electrode 50 applied as the anode in the middle of the storage container 40 has an upper cover 20. The upper cover 20, which is fixed to the coagulant discharging metal 70, the inlet 22 and the outlet 23 connected to the lid 23 and the upper strainer 24, the housing 10 and the bolt nut ( 25 is fixed to the lower cover 30 having the inlet 31 connected to the lower strainer 32 is connected to the housing 10 through the bolt nut 33 to continuously introduce the waste water to the electrical coagulation treatment It is achieved by characterized in that it can be configured.

이하, 본발명을 첨부된 도면에 의해 상세히 설명하면 다음과 같다.Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.

첨부 도면 도 1은 본 발명에 따른 전기분해를 이용한 전기응집처리 장치의단면도이고, 도 2는 본 발명의 일 실시예의 작동 상태를 나타낸 단면도이다.1 is a cross-sectional view of an electroaggregation apparatus using electrolysis according to the present invention, and FIG. 2 is a cross-sectional view showing an operating state of an embodiment of the present invention.

본 발병의 장치는 전기분해를 이용하여 폐수를 연속적으로 응집처리 시킬 수 있는 장치로서, 전원 공급부(미도시)로부터 인가되는 (+),(-) 전원과 연결되는 양극단자(53) 및 음극단자(52)와 연결되는 통전 가능한 전극판(51)과 전극봉(50)이 내장되고 전극봉(50)을 감싸 접촉되는 응집제용출금속(70) 과 통전가능한 전도성 메디아(60) 가 충진되는 반응조 하우징(10)이 갖추어져 이의 내측으로 폐수가 유입되면 응집제용출금속(70)으로부터 발생되는 양이온 금속과 전극판(51)에서 발생되는 음이온에 의해 폐수를 전기응집시켜 상부커버(20)에 구비된 배출구(21)로 배출시킴으로서 폐수를 연속적으로 응집처리하는 장치이다.The device of the present invention is a device capable of continuously coagulating wastewater by using electrolysis, and is a positive terminal 53 and a negative terminal connected to the (+), (-) power applied from a power supply (not shown) A reactor housing 10 in which an electrically conductive electrode plate 51 and an electrode rod 50 connected to the 52 are embedded and filled with a coagulant-eluting metal 70 in contact with the electrode rod 50. When the wastewater flows into the inside thereof, the wastewater is electroaggregated by the cation metal generated from the coagulant eluting metal 70 and the anion generated by the electrode plate 51 to discharge the outlet 21 provided on the upper cover 20. It is a device that continuously coagulates wastewater by discharging it.

즉 , 전기응집처리장치에 구비되는 하우징(10)은 미도시된 펌프로부터 압송된 폐수가 전기응집 처리될 수 있도록 원통형상으로 상 하부가 각각의 커버로 밀폐되도록 갖추어지며, 하부커버(30)에는 폐수를 하우징(10) 내측으로 유입시킬수 있도록 유입구(31)와 연통된 하부스트레이너(32)가 구비되고 , 아울러 이 유입구(31)을 갖춘면의 대응면 상부커버(20)에는 하우징(10)내에서 반응된 폐수를 배출시킬 수 있도록 상부스트레이너(24)와 연통된 배출구(21)가 형성된다. 이와 같이 이루어진 장치는 하우징(10)의 상부 외측에 감시창(11)과 내주벽면에는 이를 따라 그 내측면에 전극판(51)이 부착되고 전극판(51)에 부착된 음극단자(52)는 하우징(10) 외부로 돌출 되도록 하여 고정너트로 고정된다.That is, the housing 10 provided in the electrocoagulation processing apparatus has a cylindrical shape so that the upper and lower ends thereof are sealed with respective covers so that the wastewater pumped from the pump (not shown) may be electrocoagulated. The lower strainer 32 is provided in communication with the inlet 31 so as to allow the wastewater to flow into the housing 10. In addition, the upper surface 20 of the corresponding surface having the inlet 31 is provided in the housing 10. An outlet 21 is formed in communication with the upper strainer 24 so as to discharge the waste water reacted at. In the device made in this way, the monitoring plate 11 and the inner circumferential wall surface of the housing 10 are attached to the electrode plate 51 on the inner surface thereof, and the cathode terminal 52 attached to the electrode plate 51 is The housing 10 is fixed to the fixing nut so as to protrude to the outside.

한편, 양극으로 인가되는 전극봉(50)은 상부커버(20) 중앙부에 고정 너트로 고정되며, 전원공급부(미도시)와 연결되는 양극단자(53)는 상부커버 외측으로 돌출되도록 형성되며, 이 전극봉(50)과 일정한 간격을 두고 외측 둘레에는 많은 구멍들이 있는 절연체망사나 통으로 만들어진 응집제용출금속(70)이 저장되는 저장통(40)이 구비되고, 저장통(40)내에는 응집제용출금속(70) 덩어리가 충진되며, 하우징(10) 하부에는 전도성메디아(60)가 충진된다.On the other hand, the electrode rod 50 applied to the anode is fixed to the center of the upper cover 20 by a fixing nut, the positive electrode terminal 53 connected to the power supply (not shown) is formed to protrude to the outside of the upper cover, the electrode rod At a predetermined distance from the outer periphery and the outer periphery is provided with a reservoir 40 for storing the coagulant-eluting metal 70 made of an insulator mesh or a tub, and the coagulant-eluting metal 70 in the reservoir 40 is provided. Is filled, and the conductive media 60 is filled in the lower portion of the housing 10.

이때 ,전술한 전극판(51) 과 전극봉(50)은 스테인레스 재질이나 백금, 이리듐 과 같은 귀금속 물질이 코팅된 티타늄 재질로 사용함이 바람직하고, 저장통(40)에 저장되는 응집제용출금속(70)은 철이나 알루미늄 재질중 어느 것을 사용하여도 되며, 하우징(10) , 상부커버(20) 및 하부커버(30)는 전기가 통전되지 않는 절연재료로 성형함이 바람직하다.At this time, the electrode plate 51 and the electrode bar 50 described above is preferably used as a titanium material coated with a noble metal material such as stainless material or platinum, iridium, the coagulant eluting metal 70 is stored in the storage container 40 is Any one of iron and aluminum may be used, and the housing 10, the upper cover 20, and the lower cover 30 are preferably formed of an insulating material that does not conduct electricity.

하우징(10)내에 충진되는 전도성메디아(60)는 탄소 소재로 성형된 메디아 이거나 전도성 고분자 소재로 성형된 메디아로 , 크기가 1mm 이상 10mm 이하인 메디아가 적용된다.The conductive media 60 filled in the housing 10 is media formed of carbon material or media formed of conductive polymer material, and media of 1 mm or more and 10 mm or less are used.

이와 같이 이루어진 본 발병에 따른 전기응집처리장치를 이용하여 폐수를 처리시키고자 할 경우에는 도 2의 일 실시에와 같이 먼저 미도시된 펌프를 이용하여 폐수를 하부커버(30)에 구비된 유입구(31)와 연결된 하부스트레이너(32)를 통해 하우징(10)내로 유입시킨다.When the wastewater is to be treated using the electrocoagulation treatment apparatus according to the present invention, the inlet provided in the lower cover 30 by using a pump not shown first as shown in FIG. 31 is introduced into the housing 10 through the lower strainer 32 connected to the.

하우징(10)내로 유입된 폐수는 전도성메디아(60)을 유동시키며, 상부로 밀어올려 전극판(51)과 저장통(40)사이에 채워지며, 일부는 저장통(40)내부로 유입되어 응집제용출금속(70)들 사이에 충진된다.Wastewater introduced into the housing 10 flows through the conductive media 60, and is pushed upward to fill the space between the electrode plate 51 and the reservoir 40, and part of the wastewater flows into the reservoir 40 to dissolve the coagulant-eluting metal. It is filled between 70.

전도성메디아(60)을 통과한 폐수는 저장통(40)내의 응집제용출금속(70)과 접촉하면서 상부스트레이너(24)를 통해 연결된 배출구(21)로 배출된다.Wastewater that has passed through the conductive media 60 is discharged to the outlet 21 connected through the upper strainer 24 while contacting the flocculant eluting metal 70 in the reservoir (40).

이때 , 전극판(51)과 전극봉(50)에 음극과 양극을 구별시켜 전원을 인가시키면, 양극으로 인가되는 전극봉(50)과 접촉되어 저장통(40)에 위치하는 응집제용출금속(70)에서는 금속이 용해되면서 금속양이온이 발생되어 금속수산화물이 생성되고 폐수속의 부유물과 응집 반응을 일으키며, 시간이 지날수록 응집제용출금속(70)의 크기가 줄어들게 되며, 양극에 접촉되는 물은 분해되어 산소와 수소이온을 생성하고, 폐수속의 염소이온은 염소가스로 물에녹아 HOCl 이되어 유기물을 산화시키고, 음극으로 인가되는 전극판(51)에서는 물이 분해되어 수소가스와 OH- 이온을 생성한다.At this time, when the negative electrode and the positive electrode are applied to the electrode plate 51 and the electrode 50, the power is applied, and the coagulant-eluting metal 70 in contact with the electrode 50 applied as the positive electrode and positioned in the storage container 40 is made of metal. As the metal cations are dissolved, metal hydroxides are generated to cause coagulation reactions with suspended solids in the wastewater, and as time passes, the coagulant-eluting metal 70 decreases in size, and water contacting the anode decomposes to form oxygen and hydrogen ions. The chlorine ions in the waste water are dissolved in water with chlorine gas to become HOCl to oxidize organic matter, and water is decomposed in the electrode plate 51 applied to the cathode to generate hydrogen gas and OH- ions.

양극에서 발생되는 금속수산화물 및 금속양이온과 폐수내의 유기물 및 음이온성분이 결합하여 음극 전극판(51)에 부착되지만, 전도성메디아(60)가 음극전극판(51) 표면에서 유동하면서 마찰을 일으키고 ,이 결과로 전극판(51)에 부착된 이물질들이 떨어지게 되어 스케일이나 이물질 부착에의한 전류효율 감소를 방지하게 된다.The metal hydroxide and metal cation generated at the anode and the organic and anion components in the waste water are combined and attached to the cathode electrode plate 51, but the conductive media 60 flows on the surface of the cathode electrode plate 51 to cause friction. As a result, foreign matters attached to the electrode plate 51 fall, thereby preventing current efficiency reduction due to scale or foreign matter adhesion.

유입된 폐수는 음극으로 하전된 전도성메디아(60)와 양극으로 하전된 응집제용출금속(70)을 경유하면서 양극인 응집제용출금속(70)의 용해로 인해 생성되는 금속양이온, 금속수산화물 및 산소 등에 의해 응집반응, 산화반응 등이 일어나게 되고, 이와 동시에 반응결과 생성되는 응집슬러지 및 부산물들은 폐수와 함께 배출구(21)로 배출된다.The introduced wastewater is agglomerated by metal cations, metal hydroxides and oxygen generated through the dissolution of the coagulant-eluting metal 70, which is the positive electrode, via the conductive medium 60 charged to the negative electrode and the coagulant-eluting metal 70 charged to the positive electrode. A reaction, an oxidation reaction, etc. occur, and at the same time, the coagulated sludge and by-products generated as a result of the reaction are discharged to the outlet 21 together with the waste water.

한편 ,응집제용출금속(70)은 시간경과에 따라 용해되어 소모되면 ,하우징(10)에 구비된 감시창(11)을 통해 확인하여, 상부커버(20)에 구비된 뚜껑(23)을 열고 투입구(22)를 통해 응집제용출금속(70)을 보충한다.On the other hand, when the coagulant dissolution metal 70 is dissolved and consumed over time, it is checked through the monitoring window 11 provided in the housing 10, open the lid 23 provided in the upper cover 20, the inlet Through 22, the flocculant eluting metal 70 is replenished.

이상에서 설명한 본 발명은 첨부된 도면에 의해 한정되는 것이 아니고, 본 발명의 기술적 사상을 벗어나지 않는 범위 내에서 여러 가지 치환, 변형 및 변경이 가능함은 본 발명이 속하는 기술 분야에서 통상의 지식을 가진 자에게 있어 명백할 것이다.The present invention described above is not limited to the accompanying drawings, and various substitutions, modifications, and changes are possible without departing from the technical spirit of the present invention. It will be obvious to you.

이와 같은 본 발명은,Such a present invention,

첫째 : 전극을 교체하지 않고 응집제용출금속(70)만을 충진 하여 운전할 수 있도록 고안되어, 전극교체에 따른 장시간 운전 중단을 해결하였으며, 운전 및 유지 보수가 쉽고 , 제작이 쉬워 장치비용 및 운전 및 유지 보수비용을 을 절감시켰다.First: It is designed to operate by filling only the coagulant eluting metal 70 without replacing the electrode, solved the long-time operation interruption due to electrode replacement, easy operation and maintenance, easy to manufacture, equipment cost and operation and maintenance Reduced costs

둘째 : 운전 중에 전도성메디아(60)의 유동으로 전극판(51)에 마찰을 주어 스케일이 부착되는 것을 방지하여 처리효율을 높였다.Second: the friction of the electrode plate 51 by the flow of the conductive media 60 during operation to prevent the scale is attached to increase the processing efficiency.

셋째 : 종래의 장치는 염성분이 낮은 폐수를 처리할 때 , 전류가 잘흐르지 않아 효율이 낮았으나, 전도성메디아(60)을 이용하여 염성분이 낮은 폐수에서도 전류 흐름을 높여 처리효율을 높였다.Third: The conventional device is low in efficiency because the current does not flow well when treating wastewater with a low salt content, but by using the conductive media (60) to increase the current flow in the wastewater with a low salt content to increase the treatment efficiency.

넷째 : 종래의 장치는 전극이 외부에 노출되어 운전시 감전의 위험이 있으나, 본 장치는 밀폐형으로 전극판(51) 이나 전극봉(50)이 외부로 노출되지 않아 운전시 안전성을 높였다.Fourth: In the conventional device, the electrode is exposed to the outside and there is a risk of electric shock during operation, but the device is hermetically sealed and the electrode plate 51 or the electrode 50 is not exposed to the outside, thereby increasing safety during operation.

Claims (3)

하우징(10) 상부 외측 벽면에 감시창(11)과 내측 벽면에 전극판(51)이 구비되고, 그 내부에 소모성 알루미늄이나 철과 같은 응집제용출금속(70)이 저장되는 저장통(40)이 구비되며, 하우징(10) 아래쪽 내부 공간에는 전도성메디아(60)가 충진되고, 저장통(40) 중앙에 구비된 전극봉(50)은 상부커버(20)에 고정되며, 상부커버(20)에는 응집제용출금속 투입구(22) 및 뚜껑(23)과 상부스트레이너(24)와 연결되는 배출구(21)가 구비되고, 하부커버(30)에는 하부스트레이너(32)와 연결되는 유입구(31)가 구비되며, 볼트너트(33)로 하우징(10)과 연결되어 폐수를 연속적으로 유입시켜 전기적으로 응집 처리할 수 있도록 구성함을 특징으로 하는 전기응집 처리 장치.The monitoring window 11 and the electrode plate 51 are provided on the inner wall of the housing 10, and the storage container 40 in which the coagulant-eluting metal 70 such as consumable aluminum or iron is stored therein is provided. The conductive medium 60 is filled in the inner space below the housing 10, and the electrode rod 50 provided at the center of the storage container 40 is fixed to the upper cover 20, and the coagulant eluting metal is disposed on the upper cover 20. An inlet port 22 and an outlet port 21 connected to the lid 23 and the upper strainer 24 are provided, and the lower cover 30 is provided with an inlet port 31 connected to the lower strainer 32, and a bolt nut (33) is connected to the housing (10), the electro-aggregation processing apparatus, characterized in that configured to be able to electrically inject the waste water continuously in the coagulation process. 제 1항에 있어서,The method of claim 1, 하우징(10)하부에 충진되는 전도성메디아(60)는 탄소 소재로 성형된 메디아나 전도성 고분자 소재로 성형된 메디아로 1mm 보다 크고 10mm보다 작은 크기인 것을 특징으로 하는 전기응집처리 장치.The conductive media 60 filled in the lower portion of the housing 10 is a media formed of a carbon material or a media formed of a conductive polymer material, wherein the media has a size larger than 1 mm and smaller than 10 mm. 제 1항에서 있어서,The method of claim 1, 저장통(40)속의 전극봉(50)과 접촉되어 양극으로 인가된 응집제용출금속(70)과 음극 전극판(51) 사이에 전도성메디아(60)가 충진 되어 운전되는 것을 특징으로하는 전기응집처리 장치.Electro-aggregation processing apparatus characterized in that the conductive medium (60) is filled and operated between the coagulant-eluting metal 70 and the negative electrode plate (51) contacted with the electrode bar (50) in the reservoir (40).
KR1020030026171A 2003-04-24 2003-04-24 Apparatus for electro-coagulative treatment with conductive media KR20040092663A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018169321A1 (en) * 2017-03-16 2018-09-20 주식회사 아모그린텍 Electrocoagulation device
KR20180106928A (en) * 2017-03-16 2018-10-01 주식회사 아모그린텍 Apparatus of electro contaminant removal

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018169321A1 (en) * 2017-03-16 2018-09-20 주식회사 아모그린텍 Electrocoagulation device
KR20180106928A (en) * 2017-03-16 2018-10-01 주식회사 아모그린텍 Apparatus of electro contaminant removal
CN110418769A (en) * 2017-03-16 2019-11-05 阿莫绿色技术有限公司 Coagulation acquisition means
US11795073B2 (en) 2017-03-16 2023-10-24 Amogreentech Co., Ltd. Electrocoagulation device

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