KR200223758Y1 - Water treatment system using the electrical principle - Google Patents

Water treatment system using the electrical principle Download PDF

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KR200223758Y1
KR200223758Y1 KR2020000035334U KR20000035334U KR200223758Y1 KR 200223758 Y1 KR200223758 Y1 KR 200223758Y1 KR 2020000035334 U KR2020000035334 U KR 2020000035334U KR 20000035334 U KR20000035334 U KR 20000035334U KR 200223758 Y1 KR200223758 Y1 KR 200223758Y1
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electrode plate
water
water treatment
treatment apparatus
treatment
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최용관
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주식회사삼안건설기술공사
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Abstract

본 고안은 전기적원리를 이용한 수처리장치에 있어서, 처리대상원수의 전극판과의 접촉면적을 극대화시키기 위하여 전극판의 형태를 미로형으로 제작하여 설치하였으며, 전극판의 교체시에도 상부에서 전극판을 쉽게 들어올리도록 고안하여, 전극판의 교체가 손쉽게 이루어질뿐만 아니라 처리효율의 향상을 도모할 수 있도록 하였다.The present invention is a water treatment apparatus using the electrical principle, in order to maximize the contact area with the electrode plate of the raw water to be processed to install the shape of the electrode plate in the labyrinth shape, even when replacing the electrode plate in the upper electrode plate It is designed to be easily lifted, so that the electrode plate can be easily replaced and the treatment efficiency can be improved.

본 고안에 따른 전기적원리를 이용한 수처리장치의 구성은 균일간격으로 수처리장치내에 엇갈리게 설치된 스테인레스 재질로 된 미로형태의 전극판(15) 사이를 통하여 처리대상원수가 수처리장치의 후단으로 이동하는 과정에서 전극판(15)의 (+)극과 (-)극의 상호 작용에 의한 물속의 양이온, 음이온과 결합하여 응집침전 현상이 발생하게 되며, 응집침전과정에서 생긴 슬러지는 슬러지침전부(2)에 포집되어 슬러지배출관(11)을 통해 제거되게 된다. 원활한 전기적반응을 일으키기 위해 주기적으로 전류공급단자(16)를 통해 (+)극과 (-)를 번갈아 공급해주는 방식보다는 전극판(15)을 (+)극과 (-)극을 구분 하여 설치한 후 항상 일정하게 전류를 공급해주는 것이 처리효율 향상을 위해 바람직하다.The configuration of the water treatment apparatus using the electrical principle according to the present invention is the electrode in the process of moving the raw water to the rear end of the water treatment apparatus between the maze-shaped electrode plate 15 made of stainless steel staggered in the water treatment apparatus at uniform intervals Agglomeration sedimentation phenomenon occurs by combining with cations and anions in water by the interaction between the (+) and (-) poles of the plate 15, and the sludge generated during the coagulation sedimentation process is collected in the sludge sedimentation part 2. It is removed through the sludge discharge pipe (11). The electrode plate 15 is installed separately from the positive and negative electrodes rather than the alternating supply of the positive and negative poles through the current supply terminal 16 in order to cause a smooth electrical reaction. Always supplying a constant current afterwards is desirable to improve processing efficiency.

Description

전기적 원리를 이용한 수처리장치 {Water treatment system using the electrical principle}Water treatment system using the electrical principle

현재까지 전기적원리를 이용한 수처리장치는 처리효율 검증미흡 및 공사비의 증가로 인한 문제점으로 인해 적용실적이 그다지 많지 않은 실정에 있으며 특히 최소의 단위면적을 갖는 다수의 전극판을 사용하여 최대의 처리 표면적으로 처리효율을 극대화시키는 문제점을 해결해야 하는 문제점을 안고 있다.Until now, the water treatment device using electric principle has not applied much due to the problems caused by insufficient treatment efficiency verification and the increase of construction cost. Especially, the maximum treatment surface area is achieved by using a large number of electrode plates with the minimum unit area. There is a problem to solve the problem of maximizing the processing efficiency.

근래에 들어 생활수준의 향상은 용수사용량이 급증을 초래하였고 이에따라 용수부족 현상이 발생되었다. 따라서 부족분의 용수를 해결하기 위하여 오.폐수를 처리하여 화장실 등의 중수도용으로 사용할 수 있도록 시도되고 있는 바, 종래 생물학적 처리공법은 반응속도가 느릴 뿐만 아니라 처리효율이 떨어져 중수도용으로 사용하기 곤란한 문제점이 있어 별도의 고도처리시설을 구비해야 하는 문제점이 있었다.In recent years, the improvement of living standards has led to a sharp increase in water use, which has led to water shortages. Therefore, in order to solve the shortage of water, it has been attempted to be used for heavy water treatment such as toilets by treating wastewater, and the conventional biological treatment method is difficult to use for heavy water due to low reaction rate and low treatment efficiency. There was a problem to be equipped with a separate advanced processing facility.

따라서, 최근에는 상기 생물학적 처리공법 보다 처리효율 및 처리속도가 뛰어나 부족한 생활용수 및 공업용수로도 사용가능한 물리·화학적 처리방법 위주로 중점적으로 연구되고 있는 실정이며, 그 중에서도 전기적원리를 이용한 수처리방법이 부각되고 있는 실정이다.Therefore, in recent years, the treatment efficiency and treatment speed is superior to the biological treatment method, and the situation has been mainly focused on the physical and chemical treatment methods that can be used as insufficient for domestic water and industrial water, and among them, the water treatment method using electrical principles is highlighted. There is a situation.

통상의 전기적 원리를 이용한 수처리방법을 개략적으로 설명하면 먼저, 보다큰 효율을 가질 수 있도록 처리하고자 하는 처리수를 전처리 공정인 조정조에 투입시킨 후 가성소다, 무기응집제 및 적절한 첨가제(NaCl , Na2so4)등을 넣고 혼합하여 전도성을 조정하는 단계를 거치게 한다.If the water treatment method using the conventional electrical principle is outlined, first, the treated water to be treated in order to have a greater efficiency is put into a control tank, which is a pretreatment process, caustic soda, inorganic coagulant and appropriate additives (NaCl, Na2so4), etc. Add and mix to go through the steps of adjusting the conductivity.

반응기 내부로 유입된 처리대상원수는 전극판 사이를 통과하면서 전기반응을 일으키며, 이러한 전기반응은 주로 다음의 반응에 의해서 일어나며 그것은 응집(coagulation), 부상(flotation), 산화(oxidation)등 이다.The treated raw water introduced into the reactor generates an electric reaction as it passes between the electrode plates, and this electric reaction is mainly caused by the following reaction, which is coagulation, floatation, and oxidation.

이중 산화(oxidation)와 응집(coagulation)은 수처리 이론중 가장 핵심적 반응이며 산화(oxidation) 과정은 전극판의 (+)극중의 금속형태의 철이 +2 또는 +3가의 이온상태로 산화되며, 음극에서 발생된 수산화 이온(OH-)이 산화되면서 산소(O2)가 발생된다. 이렇게 발생된 산소(O2)는 유기물의 간접적인 산화(indirectoxidation)에 관여하며 이와 동시에 전극판의 음극에서는 환원이 일어나 중성조건에서 수산화 이온(OH-), 산성조건에서 수소(H2) 가스가 발생된다.Double oxidation and coagulation are the most important reactions in the theory of water treatment. The oxidation process involves the oxidation of iron in the form of metal in the positive electrode of the electrode plate to +2 or + trivalent ions. Oxygen (O2) is generated as the generated hydroxide ions (OH-) are oxidized. Oxygen (O2) generated in this way is involved in indirect oxidation of organic materials, and at the same time, reduction occurs at the cathode of the electrode plate to generate hydroxide ions (OH-) under neutral conditions and hydrogen (H2) gas under acidic conditions. .

한편, (+)극에서 용출된 금속이온은 수중의 pH 조건에 따라 산성 또는 중성의 조건에서 (+)전하를 띤 금속수화물 복합체를 형성하며, 강알칼리성 조건에서 (-)전하를 띤 금속수화물 복합체를 형성하게 된다. 따라서 일반적으로 유입 오폐수의 pH가 중성 또는 약산성 조건에서 운전이 되므로 (+)전하를 띤 금속수화물 복합체와 (-)전하를 띤 유기오염물질인 콜로이드(Colloid)의 표면전하를 전기적으로 중화시켜 이중층압축(Double layer compression)에 의한 응집을 통해 유기물이 응집 침전된다.On the other hand, the metal ions eluted at the (+) electrode form a metal hydrate complex with a (+) charge under acidic or neutral conditions, depending on the pH conditions in the water, and a metal hydrate complex with a (-) charge under strongly alkaline conditions. Will form. Therefore, in general, the pH of the influent wastewater is operated under neutral or weakly acidic conditions. Therefore, the double layer compression is performed by electrically neutralizing the surface charges of the metal hydrate complex with (+) charge and the colloid (Colloid) with (-) charge. Organic matter coagulates and precipitates through coagulation by double layer compression.

처리과정에서 생성된 응집침전물은 처리조 하부에 위치한 일정정도의 구배를 가지는 슬러지침전부로 침강되며, 침강수집된 슬러지는 주기적으로 슬러지배출관을 통해 펌프로 배출시킨다.The flocculation sediment produced during the treatment is settled to the sludge settling portion having a certain degree of gradient located in the lower part of the treatment tank, and the sediment collected sludge is periodically discharged to the pump through the sludge discharge pipe.

한편, 전극판의 산화·환원과정 중에 발생되는 기포(gas bubble)에 의해 응집된 물질이 부착되어 부유성 스컴(scum)이 발생되며, 부유성 스컴은 처리조에서 처리된 처리수와 함께 처리조 다음에 위치한 부상분리조로 유입되며 이는 상부에 떠오른 부유성스컴이 월류웨어를 넘어 스컴유출부으로 이동, 스컴배출관을 통해 부상분리조로 이동되며 처리수는 상부에 위치한 처리수배출관을 통해 처리된다On the other hand, a flocculated substance is formed by agglomerated matter by gas bubbles generated during oxidation and reduction of the electrode plate, and a floating scum is generated, and the floating scum is treated with the treated water in the treatment tank. It flows into the floating separation tank located next, and the floating scum floating at the top is moved to the scum outlet through the overflowware, and the scum discharge pipe is moved to the floating separation tank, and the treated water is treated through the treatment water discharge pipe located at the upper part.

전기적인 반응에 의해 처리대상원수가 처리되면서 상기 각 전극판은 일정사용기간이 지나게 되면 교체하여야 하며, 상호 겹쳐져 있는 각 전극판을 처리조에서 이탈시키고 삽입시켜야 하는 교체과정이 매우 불편할 뿐만 아니라 그에 따른 많은 추가 비용이 소요되는 문제점이 발생하였다.As the raw water is treated by the electrical reaction, each electrode plate must be replaced after a certain period of use, and the replacement process of removing and inserting the overlapping electrode plates from the treatment tank is very inconvenient and accordingly Many additional costs have arisen.

또한 상기한 종래의 전기적원리를 이용한 수처리장치에 있어서의 처리효율은 원통형상으로 겹쳐지게 형성된 각 전극판의 폭과 길이에 비례함에 따라 겹쳐지는 각 전극판을 넓은 폭을 갖도록 형성시킴은 물론 길이를 길게 함으로써, 처리효율을 향상시킬 수 있었으나, 그로 인한 수처리장치의 전체적인 크기가 커지게 되어(scale up) 설치상에 많은 문제점이 발생됨은 물론 설치비용이 증가되는 문제점이 초래되었다.In addition, in the water treatment apparatus using the conventional electrical principle, the treatment efficiency is formed to have a wide width as well as the length of each overlapping electrode plate in proportion to the width and length of each electrode plate formed to overlap in a cylindrical shape. By lengthening, it was possible to improve the treatment efficiency, but the overall size of the water treatment apparatus is increased (scale up), causing a lot of problems in the installation, as well as the problem that the installation cost is increased.

이에 본 고안은 상기한 종래의 문제점을 해결하기 위하여 안출한 것으로서 종래의 원통형 전극판을 평판형의 미로형태로 된 전극판으로 대체하여 전극판의 표면적을 최대한 확장시켜 물과 전극판과의 접촉표면적을 최대화 시킬 수 있는 유로구조를 채택함으로서 수처리 효율을 향상시킴을 목적으로 하는 전기적 원리를 이용한 수처리장치를 제공하는 것을 목적으로 한다.Therefore, the present invention was devised to solve the above-described problems, and replaced the conventional cylindrical electrode plate with an electrode plate in the form of a labyrinth, expanding the surface area of the electrode plate to the maximum, thereby contacting the water with the electrode plate. It is an object of the present invention to provide a water treatment apparatus using an electrical principle for the purpose of improving the water treatment efficiency by adopting a flow path structure that can maximize the flow rate.

도 1은 본 고안에 의한 전기적 수처리장치를 나타낸 절개사시도1 is a perspective view showing an electrical water treatment apparatus according to the present invention

도 2는 본 고안에 따른 전기적 수처리장치를 나타낸 입체사시도Figure 2 is a perspective view showing an electrical water treatment device according to the present invention

도 3은 본 고안에 따른 양극판과 음극판의 조립상태를 나타낸 극판상태도3 is a state of the pole plate showing the assembled state of the positive electrode plate and the negative electrode plate according to the present invention

** 도면의 주요 부분에 대한 부호의 설명 **** Description of symbols for the main parts of the drawing **

1 : 처리수유입방향 2 : 슬러지침전부1: Treatment water inflow direction 2: Sludge precipitate

3 : 제1극판 4 : 제2극판3: first electrode plate 4: second electrode plate

5 : 제3극판 6 : 제4극판5: third electrode plate 6: fourth electrode plate

7 : 제5극판 8 : 제6극판7: fifth electrode plate 8: sixth electrode plate

9 : 월류웨어 10 : 처리수유출관9: WALLWEAR ware 10: Treatment water outflow pipe

11 : 슬러지배출관 12 : 슬러지침전구멍11: sludge discharge pipe 12: sludge settling hole

13 : (+)극 전류공급선 14 : (-)극 전류공급선13: (+) pole current supply line 14: (-) pole current supply line

15 : 전극판 16 : 전류공급단자15: electrode plate 16: current supply terminal

상기의 목적을 달성하기 위해 통상의 전기적원리를 이용한 수처리장치와 같이, 본 장치도 처리대상원수의 입자상물질을 처리조 전단계에서 제거하기 위한 조치로서 유입 대상원수를 수처리장치 전단계에 설치된 조정조에 일시 저장하여 침전시킨후, 가성소다, 무기응집제, pH 조정용제를 내산성이 있는 저장탱크로 부터 약품 정량주입펌프를 통하여 처리대상원수 조정조 내부로 공급한다.Like the water treatment apparatus using the conventional electrical principle to achieve the above object, this apparatus also temporarily stores the inflow target raw water in the adjustment tank installed in the previous stage of the water treatment apparatus as a measure to remove particulate matter of the raw water to be treated. After precipitation, caustic soda, inorganic coagulant, and pH adjusting solvent are supplied from the storage tank with acid resistance to the inside of the raw water treatment tank through the chemical injection pump.

조정조에는 적은용량의 교반기를 설치하여 공급된 약품과 유입오폐수가 완전 혼합하도록 유도하며, 이렇게 약품과 혼합된 처리대상원수는 유입펌프를 통하여 본 고안의 주처리장치인 수처리장치내로 유입되게 된다.In the adjusting tank, a small amount of agitator is installed to induce the mixing of the supplied chemical and the influent waste water, and the raw water to be mixed with the chemical is introduced into the water treatment device, which is the main treatment device of the present invention, through the inlet pump.

상기의 처리수 분배장치에 의해 수처리장치내로 유입된 처리대상원수는 도 1에 도시된바와 같이 균일간격으로 수처리장치내에 엇갈리게 설치된 스테인레스 재질로 된 미로형태의 전극판(15) 사이를 통하여 수처리장치의 후단으로 이동하는 과정에서 상기에서 언급한 전극판(15)의 (+)극과 (-)극의 상호작용에 의한 물속의 양이온, 음이온과 결합하여 응집침전 현상이 발생하게 되며, 이들 발생슬러지는 슬러지침전부(2)에 포집되어 슬러지배출관(11)을 통해 제거되게 된다.The raw water to be introduced into the water treatment apparatus by the treatment water distribution apparatus is disposed between the electrode plate 15 of the labyrinth type stainless material alternately installed in the water treatment apparatus at uniform intervals as shown in FIG. 1. In the process of moving to the rear stage, the coagulation and precipitation phenomenon occurs by combining with cations and anions in water by the interaction between the (+) and (-) electrodes of the electrode plate 15 mentioned above. It is collected in the sludge settling portion 2 is removed through the sludge discharge pipe (11).

원활한 전기적반응을 일으키기 위해 주기적으로 전류공급단자(16)를 통해 (+ )극과 (-)를 번갈아 공급해주는 방식보다는 전극판(15)을 (+)극과 (-)극을 구분하여 설치한 후 항상 일정하게 전류를 공급해주는 것이 처리효율 향상을 위해 바람직하다.In order to produce a smooth electrical reaction, the electrode plate 15 is installed separately from the (+) and (-) electrodes rather than the alternating supply of the (+) and (-) through the current supply terminal 16 periodically. Always supplying a constant current afterwards is desirable to improve processing efficiency.

이에따라 본 고안 장치도 각각의 전극판(15)에 (+)극 전류공급선(13)과 (-)전류공급선(14)를 각기 설치하여 전류를 공급하였다.Accordingly, the device of the present invention also provided a current by installing a positive electrode current supply line 13 and a negative current supply line 14 on each electrode plate 15, respectively.

전극판(15)은 수처리장치 내쪽면 벽에 전극판(15)의 두께만큼 일정하게 홈을내어 삽입시킨후 설치되며, 전극판(15)의 고정은 자동적으로 처리조의 삽입과 더불어 이루어지게 된다.The electrode plate 15 is installed after inserting the grooves uniformly by the thickness of the electrode plate 15 on the inner wall of the water treatment device, and the fixing of the electrode plate 15 is automatically made with the insertion of the treatment tank.

이하, 본 고안의 바람직한 실시예를 첨부된 도면에 의해 좀더 상세하게 설명하면 다음과 같다.Hereinafter, with reference to the accompanying drawings, preferred embodiments of the present invention in more detail as follows.

도 1은 본 고안에 의한 전기적 수처리장치를 나타낸 절개사시도이며, 도 2는본 고안에 따른 전기적 수처리장치를 나타낸 입체사시도, 도 3은 본 고안에 따른 양극판과 음극판의 조립상태를 나타낸 전극판 상태도를 도시하고 있다.1 is a cutaway perspective view showing an electrical water treatment device according to the present invention, Figure 2 is a three-dimensional perspective view showing an electrical water treatment device according to the present invention, Figure 3 shows an electrode plate state diagram showing the assembled state of the positive electrode plate and the negative electrode plate according to the present invention Doing.

상기한 본 고안의 처리장치는 전단부 일측에 조정과정을 거친 처리수를 유입시키기 위한 처리수유입관이 형성되며, 상부 일측면에는 전극판을 통과한 처리수가 외부로 배출될 수 있도록 처리수배출관(10)이 형성되며, 하부에는 상기 전기적원리에 의해 발생된 침전물을 처리하기 위한 슬러지배출관(11)이 구비된다.The treatment apparatus of the present invention has a treatment water inlet pipe for introducing the treatment water undergoing the adjustment process on one side of the front end portion, and the treatment water discharge pipe to allow the treated water passing through the electrode plate to be discharged to the outside on one side thereof. 10) is formed, the lower is provided with a sludge discharge pipe 11 for treating the sediment generated by the electrical principle.

수처리장치의 외측면에는 전극판(15)에 전류를 공급할 수 있게끔 전류공급단자(16)를 설치하여 전극판(15)에 (+)극과 (-)극 전기를 공급하게 된다.On the outer surface of the water treatment apparatus, a current supply terminal 16 is installed to supply current to the electrode plate 15 to supply positive and negative electrodes to the electrode plate 15.

또한, 상기 처리장치의 하부에 형성된 슬러지침전부(2)에 슬러지가 원활히 포집될 수 있게끔 수처리장치의 하부 형태를 유출부로 갈수록 경사지게 형성하여 설치하는 것이 바람직하며, 수처리장치의 하부 경사각도에 따라 슬러지의 포집 효율이 달라지게 된다.In addition, it is preferable to install the lower form of the water treatment device to be inclined toward the outlet so that sludge can be smoothly collected in the sludge settling portion 2 formed in the lower portion of the treatment device, the sludge according to the lower inclination angle of the water treatment device The collection efficiency of is different.

이를 좀더 자세히 상술하면, 도 1에 도시된바와 같이 조정조에서 전처리단계를 거친 처리수는 상기 수처리장치의 전단에 형성된 원수유입관을 통하여 수처리장치에 유입되어지고, 수처리장치내로 유입된 처리대상원수는 처리조내에 단계별로 설치되어진 전극판(15)을 지나면서 상기에서 언급한 전기적반응에 의해 응집침전과정을 거치게 된다.In more detail, as shown in FIG. 1, the treated water that has undergone the pretreatment step in the adjustment tank is introduced into the water treatment apparatus through a raw water inlet pipe formed at the front end of the water treatment apparatus, and the target water introduced into the water treatment apparatus is Passing the electrode plate 15 installed step by step in the treatment tank is subjected to the coagulation sedimentation process by the above-mentioned electrical reaction.

처리수는 도 2에 도시된바와 같이 처리조내에 다수개가 설치되어 있는 전극판(15)을 통과하면서, 즉 상기 미로형태로 구성되어진 전극판(15) 사이를 지나면서 (+)극과 (-)극에 의한 응집침전작용을 일으켜서 처리수에 함유되어 있는 불순물이 제거되는 것이다.As shown in FIG. 2, the treated water passes through the electrode plate 15 provided with a plurality in the treatment tank, that is, passes between the electrode plate 15 constituted in the labyrinth and the (+) electrode and (- This causes coagulation and sedimentation action by the electrode to remove impurities contained in the treated water.

상기와 같이 모든 전극판(15)을 통과한 처리수는 수처리장치의 후단 상부에설치된 처리수유출관(10)을 거쳐 외부로 배출되어지고, 처리수중에 함유되어 있 불순물은 전기반응에 의한 응집침전후 처리조 하부에 형성된 슬러지침전부(2)에 집적된 후 슬러지배출관(11)을 통하여 외부로 배출되어 진다.As described above, the treated water that has passed through all the electrode plates 15 is discharged to the outside through the treated water outlet pipe 10 installed at the rear end of the water treatment apparatus, and the impurities contained in the treated water are flocculated and precipitated by electric reaction. After being integrated in the sludge settling portion 2 formed in the lower part of the after-treatment tank is discharged to the outside through the sludge discharge pipe (11).

이상 설명한 바와 같이, 본 고안에 따른 전기적 원리를 이용한 수처리장치는전극판을 미로형태로 제작하여 처리대상원수와의 접촉면적을 최대한 확장시킴으로서 동일 처리조 면적에서 최대의 수처리 효율을 기대할 수가 있다.As described above, the water treatment apparatus using the electrical principle according to the present invention can be expected to maximize the water treatment efficiency in the same treatment tank area by making the electrode plate in the maze form to maximize the contact area with the raw water to be treated.

또한 본 고안은 기존의 물리·화학적처리 및 생물학적처리 보다 처리효율이향상되고, 체류시간이 짧아 반응속도가 빠르며, 전극판의 부식은 그다지 나타나지 않아 최소 5년 이상 전극판의 원형이 유지될 것으로 판단되며, 따라서 전극판의 교체비용이 적게 소모되어 처리시설 유지관리비용이 적게 소요될 것으로 판단된다.In addition, the present invention improves the treatment efficiency than the existing physical and chemical treatments and biological treatments, and the reaction time is faster due to the short residence time, and the corrosion of the electrode plate does not appear so that the prototype of the electrode plate will be maintained for at least five years. Therefore, the replacement cost of the electrode plate is consumed less, and therefore, the maintenance cost of the treatment facility is expected to be less.

아울러 본 고안에 따른 전기적 원리를 이용한 수처리장치는 무기응집제의 투여와 3차원적 전극효과에 의해 산화·환원작용이 배가되어 단시간내에 처리대상원수의 오염물질들이 분해되고, 침전성 입자상 물질의 유동을 층유화시켜 균일하게 분배시키는 처리조 내부에서 침전배출되어 후단의 부상분리조에서 침전부하를 감소시킬 수 있는 고도처리장치를 제공할 수 있다.In addition, the water treatment apparatus using the electrical principle according to the present invention doubles the oxidation / reduction effect by the administration of the inorganic coagulant and the three-dimensional electrode effect, so that contaminants of the target water are decomposed within a short time, and the flow of precipitated particulate matter is reduced. It is possible to provide an advanced treatment apparatus capable of reducing the settling load in the flotation tank at the rear end by discharging the sediment in the treatment tank uniformly distributing the bed.

Claims (1)

정사각형 형태의 전기적원리를 이용한 수처리장치에 있어서; 처리대상원수를처리하기 위한 스테인레스재질로 된 격자형 미로형태의 전극판(15)이 처리조내에 다수개가 구비되며; 이들 전극판(15)에 전기를 공급하기 위한 전류공급단자(16)가설치되어 (+)극과 (-)극을 구분해서 전극판에 공급해주며; 수처리장치 하부에는 응집침전된 슬러지를 배출시키기 위한 슬러지배출관(11)을 구비하여 된 것을 특징으로 하는 전기적 원리를 이용한 수처리장치In the water treatment apparatus using a square-type electrical principle; A plurality of lattice-shaped labyrinth-shaped electrode plates 15 for treating raw water to be treated are provided in the treatment tank; A current supply terminal 16 for supplying electricity to these electrode plates 15 is provided so as to separate the (+) and (-) electrodes and supply them to the electrode plate; The water treatment apparatus using the electrical principle, characterized in that the lower portion of the water treatment device is provided with a sludge discharge pipe 11 for discharging the flocculated sediment.
KR2020000035334U 2000-12-16 2000-12-16 Water treatment system using the electrical principle KR200223758Y1 (en)

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