KR20040088870A - Apparatus and method for purifying water through an electrical adsorption-desorption cycle using an activated carbon electrode with both positive and negative - Google Patents
Apparatus and method for purifying water through an electrical adsorption-desorption cycle using an activated carbon electrode with both positive and negative Download PDFInfo
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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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
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
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Abstract
Description
본 발명은 양음극 동형 활성탄소전극을 이용한 전기흡탈착식 물 정화장치 및 이 장치를 이용한 물 정화방법에 관한 것이다. 더욱 상세하게, 본 발명은 전기화학적 방법에 의한 물 정화장치 및 방법으로서, 0.1 내지 2.0 볼트의 전압을 활성탄소전극에 인가하여 이온교환막을 통하여 산업폐수, 해수, 기수 등으로부터 무기이온을 빠르게 활성탄소전극에 흡착시킨 후, 같은 전압을 반대로 인가하여 이온교환막의 역할에 따라 흡착은 방지하고, 흡착된 이온만을 빠르게 탈착시켜 물 중의 무기이온을 제거할 수 있는 양음극 동형 활성탄소전극을 이용한 전기흡탈착식 물 정화장치 및 이 장치를 이용한 물 정화방법에 관한 것이다.The present invention relates to an electroadsorption-and-desorption water purification device using a cathode positive active carbon electrode and a water purification method using the device. In more detail, the present invention is an apparatus and method for purifying water by an electrochemical method, which rapidly converts inorganic ions from industrial wastewater, seawater, brackish water, etc. through an ion exchange membrane by applying a voltage of 0.1 to 2.0 volts to an activated carbon electrode. After adsorption on the electrode, the same voltage is reversed to prevent adsorption according to the role of the ion exchange membrane, and the electrosorption and desorption type using a cathode-cathodic active carbon electrode capable of quickly desorbing only the adsorbed ions to remove inorganic ions in water. A water purification device and a water purification method using the device.
일반적으로 대용량의 물을 정화하는 방법에는 이온교환수지법, 역삼투막법, 증발법 등이 있으나 고에너지소비, 2차 오염물 발생, 유지관리의 곤란 등 많은 단점을 가지고 있다.Generally, there are many methods for purifying a large amount of water, such as ion exchange resin method, reverse osmosis membrane method, evaporation method, etc., but there are many disadvantages such as high energy consumption, secondary pollutant generation, and difficulty in maintenance.
대용량의 물을 정화하기 위하여 에너지소비량을 줄이고 2차 환경오염을 줄이며 유지관리를 편리하게 하는 것이 과제이다. 이러한 문제해결을 위해 전기흡탈착 원리를 이용한 정화방법이 시도되고 있다.In order to purify a large amount of water, the task is to reduce energy consumption, reduce secondary environmental pollution, and make maintenance easier. In order to solve this problem, a purification method using the electrosorption principle has been attempted.
그러나, 전기흡탈착 원리를 이용한 정화방법도 직렬 다단 반응기를 이용할 경우 빠른 흡탈착속도와 탈착과정의 고효율이 요구되고 있는 실정이다.However, the purification method using the electrosorption and desorption principle also requires a fast adsorption and desorption rate and a high efficiency of the desorption process when using a serial multistage reactor.
이에 본 발명은 산업폐수, 해수, 기수 등의 고 무기염을 함유하고 있는 물로부터 무기이온의 제거속도를 높이고, 전극의 재생효율을 높일 수 있는 양음극 동형 활성탄소전극을 이용한 대용량 전기흡탈착식 물 정화장치와 이 장치를 이용한 물 정화방법을 제공하는데 그 목적이 있는 것이다.Accordingly, the present invention provides a high-capacity electrosorption and desorption water using a cathode-cathodic active carbon electrode that can increase the removal rate of inorganic ions from water containing high inorganic salts such as industrial wastewater, seawater, and brackish water, and improve the regeneration efficiency of the electrode. It is an object of the present invention to provide a purification device and a water purification method using the device.
도 1은 본 발명의 대용량 전기흡탈착식 물 정화장치의 전체 공정도이다.1 is an overall process diagram of a large-capacity electroadsorbable water purification device of the present invention.
도 2는 도 1에서의 정화반응기의 입체 사시도이다.FIG. 2 is a three-dimensional perspective view of the purification reactor in FIG. 1.
도 3은 도 1의 정화반응기의 평면도이다.3 is a plan view of the purification reactor of FIG.
도 4는 도 1의 정화반응기의 정면도이다.4 is a front view of the purification reactor of FIG.
도 5는 도 1의 정화반응기의 측면도이다.5 is a side view of the purification reactor of FIG. 1.
도 6은 도 1의 정화반응기에서의 유체흐름도이다.6 is a flow chart of the purification reactor of FIG.
<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>
10 : 정화반응기 12 : 직류전원공급장치10: purification reactor 12: DC power supply
14 : 음전압인가선 16 : 양전압인가선14: negative voltage supply line 16: positive voltage supply line
18 : 유체관 20 :음극집전체18: fluid tube 20: negative electrode current collector
22 : 음전극 24 : 양이온교환막22: negative electrode 24: cation exchange membrane
26 : 스페이서 28 : 음이온교환막26 spacer 28 anion exchange membrane
30 : 양전극 32 : 양극집전체30 positive electrode 32 positive electrode current collector
본 발명의 양음극 동형 활성탄소전극을 이용한 대용량 전기흡탈착식 물 정화장치는 0.1 내지 2.0볼트의 음전압과 양전압을 인가하기 위한 전원공급장치; 상기 전원공급장치와 연결되어 있으면서 물 중의 무기이온을 양이온과 음이온으로 각각 흡착한 후 탈착시켜 제거하는 활성탄소전극을 갖는 정화반응기가 하나 또는 그 이상으로 연결되어 설치된 것을 특징으로 한다.Large-capacity electrosorption-and-desorption water purification apparatus using the positive-cathode active carbon electrode of the present invention includes a power supply for applying a negative voltage and a positive voltage of 0.1 to 2.0 volts; While connected to the power supply device is characterized in that the purifying reactor having an activated carbon electrode for adsorbing the inorganic ions in the water with cations and anions, respectively, and then desorption to remove one or more.
본 발명에서 상기 정화반응기는 물이 흐르게 되는 스페이서, 상기 양전압 및 음전압 인가선과 연결되어 있으면서 양이온과 음이온을 흡착하게 되는 양전극 및 음전극의 활성탄소전극, 물 중의 양이온과 음이온 만을 선택적으로 통과시키게 되는 양이온 및 음이온 교환막, 탄소 호일로 구성된 양극 및 음극 집전체로 구성되어 있다.In the present invention, the purification reactor selectively passes only the positive and negative ions in the active carbon electrode of the positive electrode and the negative electrode, which is connected to the spacer, the positive and negative voltage applied lines through which water flows and adsorbs positive and negative ions. It consists of a positive and negative electrode current collector which consists of a cation and anion exchange membrane, and carbon foil.
또한, 본 발명의 양음극 동형 활성탄소전극을 이용한 대용량 전기흡탈착식 물 정화방법은 전원공급장치로부터 0.1 내지 2.0볼트의 양전압과 음전압을 무기이온을 함유하는 물이 흐르는 정화반응기에 인가하고, 상기 정화반응기에서 전압이 인가된 양전극과 음전극에서 물 중의 무기이온을 선택적으로 흡착하도록 한 후, 무기이온이 각 전극에 흡착포화되면 이들에 반대 전압을 인가하여 다시 탈착되도록하여 무기이온을 제거하는 공정을 직렬로 연결된 정화반응기를 이용하여 다단계로 반복해서 실시하는 것을 특징으로 한다.In addition, the large-capacity electroabsorbable water purification method using the positive-cathode active carbon electrode of the present invention applies a positive voltage and a negative voltage of 0.1 to 2.0 volts from the power supply to the purification reactor flowing water containing inorganic ions, In the purification reactor, the positive and negative electrodes to which voltage is applied are selectively adsorbed, and when inorganic ions are saturated and adsorbed on each electrode, a reverse voltage is applied to them to remove and desorb inorganic ions. It is characterized in that it is carried out repeatedly in multiple stages using a purification reactor connected in series.
본 발명의 방법에서, 상기 양전극 및 음전극에 대한 무기이온의 흡착은 양이온 교환막 및 음이온교환막을 매개로 하여 이루어지도록 하고, 탈착은 반대 전압의 인가로 인해 이들 이온교환막을 통과하지 못하도록 하여서 실시하는 것을 특징으로 한다.In the method of the present invention, the adsorption of inorganic ions to the positive electrode and the negative electrode is carried out through the cation exchange membrane and the anion exchange membrane, and the desorption is carried out by preventing the passage of these ion exchange membrane due to the application of the reverse voltage. It is done.
이와 같은 본 발명을 첨부도면에 의거하여 더욱 상세하게 설명하기로 한다.This invention will be described in more detail based on the accompanying drawings.
첨부 도면 중 도 1은 본 발명의 대용량 전기흡탈착식 물 정화장치의 배치상태를 보여주기 위한 개략도로서, 도 1에 의하면, 본 발명의 대용량 전기흡탈착식 물 정화장치는 물 중의 무기이온을 양이온과 음이온으로 각각 흡착한 후 탈착제거하는 정화반응기(10), 해당 정화반응기(10)에 전압을 공급하기 위한 전원공급장치 (12), 그리고, 상기 정화반응기(10)에 음전압을 인가하기 위한 음전압 인가선(14), 상기 정화반응기(10)에 양전압을 인가하기 위한 양전압 인가선(16) 등으로 구성되어 있다.Figure 1 is a schematic diagram showing the arrangement of the large-capacity electrodesorption water purification apparatus of the present invention, according to Figure 1, the large-capacity electrosorption water purification apparatus of the present invention is the inorganic ion in water cations and anions Purifying reactor 10 for desorption and removal of the respective adsorptions, power supply device 12 for supplying voltage to the purifying reactor 10, and negative voltage for applying a negative voltage to the purifying reactor 10. And an application line 14 and a positive voltage application line 16 for applying a positive voltage to the purification reactor 10.
도 2는 도 1에서 전기흡탈착 반응에 의하여 무기이온을 정화하게 되는 정화반응기(10)의 입체 사시도를 나타낸 것으로, 아래쪽 유체관(18)을 통해서 물이 정화반응기 내부로 유입되고, 위쪽 유체관(18)을 통해서 물이 유출되게 되어 있으며, 이에 따라 도 1에서 점선으로 나타낸 화살표 방향과 같이 물이 직렬로 연결된 여러 개의 정화반응기(10)를 반복해서 흐르게 된다.FIG. 2 is a three-dimensional perspective view of the purification reactor 10 to purify the inorganic ions by the electrosorption and desorption reaction in FIG. 1, wherein water is introduced into the purification reactor through the lower fluid tube 18, and the upper fluid tube Water 18 is to flow through, so that the water is repeatedly flowed through a plurality of purification reactors 10 connected in series as shown by the arrow in FIG.
도 3은 도 1의 정화반응기(10)의 평면도를 나타낸 것으로, 유체관(18)을 통해서는 물이 흐르게 되고, 음전압 인가선(14)을 통해서는 음전압이 전압공급장치 (12)로부터 정화반응기(10)에 인가되고, 양전압 인가선(16)을 통해서는 양전압이 인가된다.3 is a plan view of the purification reactor 10 of FIG. 1, in which water flows through the fluid pipe 18, and negative voltage is supplied from the voltage supply device 12 through the negative voltage applying line 14. A positive voltage is applied to the purification reactor 10 and a positive voltage applied through the positive voltage applying line 16.
도 4는 도 1의 정화반응기(10)의 정면도를 나타낸 것으로, 도 5는 측면도를 나타낸 것이다. 본 발명의 정화반응기(10)는 음극집전체(20), 음전극(22), 양이온교환막(24), 물흐름을 유지하기 위한 스페이서(26), 음이온교환막(28), 양전극(30), 양극집전체(32)로 구성되어 있다. 물의 처리용량에 맞게 여러 단으로 자유로이 구성요소를 증가하여 설치할 수 있다.Figure 4 shows a front view of the purification reactor 10 of Figure 1, Figure 5 shows a side view. Purification reactor 10 of the present invention is the negative electrode current collector 20, the negative electrode 22, the cation exchange membrane 24, the spacer 26 for maintaining the water flow, the anion exchange membrane 28, the positive electrode 30, the positive electrode The current collector 32 is composed of. The components can be freely increased in multiple stages to accommodate the water treatment capacity.
도 6은 정화반응기(10)내의 물의 흐름방향을 보여주기 위한 것으로 아래쪽 유체관(18)을 통해서 물이 반응기내로 유입되고 스페이서(26)을 통해서 가운데 구멍으로 이동한 후 최종 위쪽 유체관(18)을 통해서 정화반응기(10) 외부로 유출된다. 물이 스페이서(26) 내를 이동하는 중에 물 중의 양이온들은 양이온 교환막(24)을 통과하여 0.5 내지 2.0볼트의 음전압이 인가된 음전극(22)에 흡착되고 음이온들은 음이온교환막(28)을 통과하여 0.1 내지 2.0볼트의 양전압이 인가된 양전극(30)에 흡착하게 된다.FIG. 6 shows the flow direction of water in the purification reactor 10. The water flows into the reactor through the lower fluid pipe 18 and moves to the center hole through the spacer 26. Out through the purification reactor (10). As water moves in the spacer 26, cations in the water pass through the cation exchange membrane 24 and are adsorbed to the negative electrode 22 to which a negative voltage of 0.5 to 2.0 volts is applied, and anions pass through the anion exchange membrane 28. A positive voltage of 0.1 to 2.0 volts is adsorbed to the applied positive electrode 30.
이온들이 각 전극에 흡착포화되면 이 이온들을 탈착시켜 제거하는 재생공정이 이어지게 되며 이 공정에서는 흡착공정에서와는 반대로 음전극(22)에는 0.1 내지 2.0볼트의 양전압이 인가되고 양전극(30)에는 0.1 내지 2.0볼트의 음전압이 인가됨으로써 각 전극에 흡착된 이온들이 탈착되게 된다. 이 때 음이온은 양이온교환막을, 그리고 양이온은 음이온교환막을 통과할 수 없기 때문에 각 전극으로의 흡착반응은 전혀 발생하지 않게 된다. 따라서 재생효율을 극대화할 수 있다.When the ions are adsorbed and saturated on each electrode, a regeneration process of desorbing and removing these ions is continued. In this process, a positive voltage of 0.1 to 2.0 volts is applied to the negative electrode 22 and 0.1 to 2.0 volts to the positive electrode 30 as opposed to the adsorption process. When a negative voltage of is applied, ions adsorbed to each electrode are desorbed. At this time, the anion does not pass through the cation exchange membrane and the cation cannot pass through the anion exchange membrane, so that no adsorption reaction occurs to each electrode. Therefore, the regeneration efficiency can be maximized.
본 발명의 양음극 동형 활성탄소전극을 이용한 대용량 전기흡탈착식 물 정화장치 및 방법은 0.1 내지 2.0 볼트의 낮은 전기를 이용함으로서 에너지 소비량이 적고 재생시 약품을 사용하지 않아 환경오염이 없으며 유지관리가 편리하다. 수질에 따라 여러 정화반응기를 직렬로 연결하여 사용이 가능하여 수질에 맞게 구성이 용이하고 하나의 반응기내에 구성요소들을 필요처리용량에 따라 추가설치가 용이하여 대용량화하는데도 효과적이다.Large-capacity electrosorption and desorption water purification device and method using the positive-cathode active carbon electrode of the present invention uses less electricity of 0.1 to 2.0 volts, which consumes less energy and does not use chemicals during regeneration, thus eliminating environmental pollution and convenient maintenance. Do. Depending on the water quality, it is possible to connect several purification reactors in series so that it is easy to configure according to the water quality, and it is also effective to increase the capacity by easily installing components according to the required treatment capacity in one reactor.
또한, 이온교환막을 부가하여 사용함으로서 재생효율을 극대화할 수 있다. 따라서 경제적으로 고농도 무기물을 함유하는 물로부터 각종 용수를 생산하여 각 용도로 활용할 수 있는 효과가 있다.In addition, it is possible to maximize the regeneration efficiency by adding an ion exchange membrane. Therefore, it is economically effective to produce a variety of water from the water containing a high concentration of inorganic substances can be utilized for each purpose.
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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KR100762008B1 (en) * | 2006-05-29 | 2007-10-04 | (주)경인양행 | Water-treatment system of improved recovery rate |
KR100915338B1 (en) * | 2007-10-10 | 2009-09-03 | (주) 시온텍 | A structure for composing an apparatus for purifying water through an electrical adsorption-desorption cycle |
CN111646549A (en) * | 2020-06-12 | 2020-09-11 | 大连双迪创新科技研究院有限公司 | Water purifier and water purifying method thereof |
KR20200129276A (en) * | 2019-05-08 | 2020-11-18 | 최현성 | Household water purifier comprising carbon electrode filter and its controlling method |
KR20200129277A (en) * | 2019-05-08 | 2020-11-18 | 최현성 | Carbon electrode filter for household water purifier and its manufacturing method |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
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KR101094731B1 (en) * | 2009-09-30 | 2011-12-16 | 한국전력공사 | Electrochemical water treatment apparatus using carbon electrodes |
KR101282794B1 (en) | 2012-01-06 | 2013-07-05 | 한국에너지기술연구원 | Stack-type flow capacitive deionization device |
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2003
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100762008B1 (en) * | 2006-05-29 | 2007-10-04 | (주)경인양행 | Water-treatment system of improved recovery rate |
KR100915338B1 (en) * | 2007-10-10 | 2009-09-03 | (주) 시온텍 | A structure for composing an apparatus for purifying water through an electrical adsorption-desorption cycle |
KR20200129276A (en) * | 2019-05-08 | 2020-11-18 | 최현성 | Household water purifier comprising carbon electrode filter and its controlling method |
KR20200129277A (en) * | 2019-05-08 | 2020-11-18 | 최현성 | Carbon electrode filter for household water purifier and its manufacturing method |
CN111646549A (en) * | 2020-06-12 | 2020-09-11 | 大连双迪创新科技研究院有限公司 | Water purifier and water purifying method thereof |
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