CN106865701B - Electrolytic cell for seawater desalination mixed capacitor - Google Patents
Electrolytic cell for seawater desalination mixed capacitor Download PDFInfo
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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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
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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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
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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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
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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
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
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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
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
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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
- C02F2201/00—Apparatus for treatment of water, waste water or sewage
- C02F2201/46—Apparatus for electrochemical processes
- C02F2201/461—Electrolysis apparatus
- C02F2201/46105—Details relating to the electrolytic devices
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- Environmental & Geological Engineering (AREA)
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Abstract
Description
技术领域technical field
本发明属于电解池领域,尤其涉及一种用于海水脱盐混合电容的电解池。The invention belongs to the field of electrolytic cells, in particular to an electrolytic cell used for a mixed capacitor for seawater desalination.
背景技术Background technique
随着世界经济及工业的发展、人口的不断增长及环境污染的日益严重,淡水资源的需求量与日俱增。如何从占世界总储水量98%的海水和苦咸水中获得廉价的淡水在世界范围内日益受到关注。目前实现海水淡化的技术主要包括蒸馏法、反渗透法和电渗析法等方法,然而这些方法具有耗能高、产生二次污染等缺点。电容去离子技术的出现,,使人们看到了实现低耗能,无污染海水淡化的希望。With the development of the world economy and industry, the continuous growth of the population and the increasingly serious environmental pollution, the demand for freshwater resources is increasing day by day. How to obtain cheap fresh water from seawater and brackish water, which account for 98% of the world's total water storage, is a growing concern worldwide. At present, the technologies for realizing seawater desalination mainly include distillation, reverse osmosis and electrodialysis. However, these methods have disadvantages such as high energy consumption and secondary pollution. The emergence of capacitive deionization technology has made people see the hope of realizing low-energy consumption and pollution-free seawater desalination.
发明内容SUMMARY OF THE INVENTION
发明目的:本发明提供一种脱盐充分、稳定性强及结构简单的用于海水脱盐混合电容的电解池。Purpose of the invention: The present invention provides an electrolytic cell for seawater desalination hybrid capacitor with sufficient desalination, strong stability and simple structure.
技术方案:本发明用于海水脱盐混合电容的电解池,自下而上依次包括分体配套设置的带有第一凸块的池底盖、池体、设于池体内的电极及带有第二凸块的池顶盖,所述池体上开设有中空槽,第一凸块与中空槽的底端相卡合,所述第二凸块与中空槽的顶端相卡合,所述池体上分别设有进水管及出水管,该进水管及出水管分别通过其上间隔设置的若干连接孔与中空槽相连通。Technical scheme: The electrolytic cell of the present invention for the mixed capacitor of seawater desalination comprises, from bottom to top, the bottom cover of the cell with the first bump, the cell body, the electrode arranged in the The top cover of the pool with two protrusions, the pool body is provided with a hollow groove, the first protrusion is engaged with the bottom end of the hollow groove, the second protrusion is engaged with the top end of the hollow groove, the pool The body is respectively provided with a water inlet pipe and a water outlet pipe, and the water inlet pipe and the water outlet pipe are respectively communicated with the hollow groove through a plurality of connecting holes arranged at intervals on the water inlet pipe and the water outlet pipe.
进一步说,本发明池底盖及池体的之间设有具有中心通孔的第一硅胶垫片,该中心通孔与第一凸块相贴合;池体及池顶盖的之间设有具有中心通孔的第二硅胶垫片,该中心通孔与第二凸块相贴合。Further, between the pool bottom cover and the pool body of the present invention, there is a first silicone gasket with a central through hole, and the center through hole is fitted with the first bump; between the pool body and the pool top cover There is a second silicone gasket with a central through hole, and the central through hole is fitted with the second bump.
再进一步说,本发明的进水管及出水管左右对称设于池体上;电极包括阴极钠锰氧化物电极和阳极活性炭电极,该两电极之间放置有绝缘垫片。Furthermore, the water inlet pipe and the water outlet pipe of the present invention are symmetrically arranged on the tank body; the electrodes include a cathode sodium manganese oxide electrode and an anode activated carbon electrode, and an insulating gasket is placed between the two electrodes.
更进一步说,本发明第一凸块与第二凸块的高度比为1:1;第一凸块与池底盖及池体的高度比为1:1.25~1.6:2~2.8;第二凸块与池底盖及池体的高度比为1:1.25~1.6:2~2.8。Furthermore, in the present invention, the height ratio of the first bump to the second bump is 1:1; the height ratio of the first bump to the pool bottom cover and the pool body is 1:1.25-1.6:2-2.8; The height ratio of the bump to the bottom cover of the pool and the pool body is 1:1.25-1.6:2-2.8.
有益效果:与现有技术相比,本发明的显著优点为:该电解池采用分体配套设置的组合式的结构,结构简单,便于更换电极及设置于电极件的绝缘垫片,不仅能够以防短路且可重复使用,降低了生产成本。Beneficial effects: Compared with the prior art, the significant advantages of the present invention are: the electrolytic cell adopts a combined structure that is arranged in separate parts. Short-circuit proof and reusable, reducing production costs.
附图说明Description of drawings
图1为本发明用于海水脱盐混合电容的电解池的结构示意图;Fig. 1 is the structural representation of the electrolytic cell used for seawater desalination hybrid capacitor of the present invention;
图2为本发明池体的内部结构示意图;Fig. 2 is the internal structure schematic diagram of the pond of the present invention;
图3为本发明用于海水脱盐混合电容的电解池的内部结构示意图。FIG. 3 is a schematic diagram of the internal structure of the electrolytic cell used for the hybrid capacitor for seawater desalination according to the present invention.
具体实施方式Detailed ways
下面结合附图及实施例对本发明的技术方案作进一步说明。The technical solutions of the present invention will be further described below with reference to the accompanying drawings and embodiments.
如图1所示,本发明用于海水脱盐混合电容的电解池,其自下而上依次包括分体配套设置的带有第一凸块1的池底盖2、池体3、设于池体3内的电极4及带有第二凸块5的池顶盖6。As shown in FIG. 1 , the electrolytic cell of the present invention used for seawater desalination hybrid capacitors includes, from bottom to top, a
池底盖2及池体3的之间设有具有中心通孔的第一硅胶垫片10,该中心通孔与第一凸块1相贴合;池体3及池顶盖6的之间设有具有中心通孔的第二硅胶垫片11,该中心通孔与第二凸块5相贴合,分别设置第一硅胶垫片10及第二硅胶垫片11,以防止液体流出。池体3上开设有中空槽7,用来容纳氯化钠液体,第一凸块1与中空槽7的底端相卡合,第二凸块5与中空槽7的顶端相卡合,从而形成闭合空间,该池体3上还分别设有左右对称设置的进水管8及出水管9,该进水管8及出水管9分别通过其上间隔设置的若干连接孔与中空槽7相连通,如图2所示,通过设置若干个连接孔,从而减小氯化钠液体的流速,使得氯化钠液体能够充分地进行脱盐,提高脱除率。Between the
如图3所示,电极4包括阴极钠锰氧化物电极12和阳极活性炭电极13,该两电极之间放置有绝缘垫片14。采用钠锰氧化物电极具有对于高容量的氯化钠溶液的脱盐性能,其为普通去离子系统脱盐量的两倍多,且在两电极之间的绝缘垫片,基本防止了短路,并且使氯化钠溶液从电极之间流过,电极之间短路的减少,提高了电解的效率。As shown in FIG. 3 , the electrode 4 includes a cathode sodium
实施例1Example 1
池底盖2及池顶盖6的底面积均为100mm×100mm,高度均为8mm,第一凸块1及第二凸块5的底面积均为50mm×50mm,高度均为5mm,其分别位于池底盖2及池顶盖6的中间部位;第一硅胶垫片10及第二硅胶垫片11的底面积均为100mm×100mm,高度为1mm,中心通孔的面积为50mm×50mm,池体3的底面积100mm×100mm,高度为14mm,中空槽7的面积为52mm×52mm,进水管8和出水管9上等距设有12个直径1mm的连接孔,钠锰氧化物电极12的面积为50mm×50mm,活性炭电极13的面积为50mm×50mm,绝缘垫片14的面积为50mm×50mm,本发明的电解池采用有机玻璃制成。The bottom area of the
实施例2Example 2
池底盖2及池顶盖6的底面积均为100mm×100mm,高度均为8mm,第一凸块1及第二凸块5的底面积均为50mm×50mm,高度均为5mm,其分别位于池底盖2及池顶盖6的中间部位;第一硅胶垫片10及第二硅胶垫片11的底面积均为100mm×100mm,高度为1mm,中心通孔的面积为50mm×50mm,池体3的底面积100mm×100mm,高度为14mm,中空槽7的面积为52mm×52mm,进水管8和出水管9上等距设有12个直径1mm的连接孔,钠锰氧化物电极12的面积为50mm×50mm,活性炭电极13的面积为50mm×50mm,绝缘垫片14的面积为50mm×50mm,本发明的电解池采用聚四氟乙烯制成。The bottom area of the
实施例3Example 3
池底盖2及池顶盖6的底面积均为50mm×50mm,高度均为4mm,第一凸块1及第二凸块5的底面积均为25mm×25mm,高度均为2.5mm,其分别位于池底盖2及池顶盖6的中间部位;第一硅胶垫片10及第二硅胶垫片11的底面积均为50mm×50mm,高度为1mm,中心通孔的面积为25mm×25mm,池体3的底面积50mm×50mm,高度为7mm,中空槽7的面积为26mm×26mm,进水管8和出水管9上等距设有12个直径1mm的连接孔,钠锰氧化物电极12的面积为25mm×25mm,活性炭电极13的面积为25mm×25mm,绝缘垫片14的面积为25mm×25mm,本发明的电解池采用有机玻璃制成。The bottom area of the
实施例4Example 4
池底盖2及池顶盖6的底面积均为100mm×100mm,高度均为10mm,第一凸块1及第二凸块5的底面积均为50mm×50mm,高度均为8mm,其分别位于池底盖2及池顶盖6的中间部位;第一硅胶垫片10及第二硅胶垫片11的底面积均为100mm×100mm,高度为1mm,中心通孔的面积为50mm×50mm,池体3的底面积为100mm×100mm,高度为16mm,中空槽7的面积为52mm×52mm,进水管8和出水管9上等距设有12个直径1mm的连接孔,钠锰氧化物电极12的面积为50mm×50mm,活性炭电极13的面积为50mm×50mm,绝缘垫片14的面积为50mm×50mm,本发明的电解池采用有机玻璃制成。The bottom area of the
实施例5Example 5
池底盖2及池顶盖6的底面积均为100mm×100mm,高度均为6mm,第一凸块1及第二凸块5的底面积均为50mm×50mm,高度均为4mm,其分别位于池底盖2及池顶盖6的中间部位;第一硅胶垫片10及第二硅胶垫片11的底面积均为100mm×100mm,高度为1mm,中心通孔的面积为50mm×50mm,池体3的底面积100mm×100mm,高度为10mm,中空槽7的面积为52mm×52mm,进水管8和出水管9上等距设有12个直径1mm的连接孔,钠锰氧化物电极12的面积为50mm×50mm,活性炭电极13的面积为50mm×50mm,绝缘垫片14的面积为50mm×50mm,本发明的电解池采用有机玻璃制成。The bottom area of the
工作原理:首先,将池底盖2,第一硅胶垫片10与池体3边缘切合固定;其次,将钠锰氧化物电极12与活性炭电极13中间夹着绝缘垫片14边缘切合后,放入池体3中,放置第二硅胶垫片11及池顶盖6,同样边缘契合后,采用螺丝拧合形成一整体;最后将橡皮管插入进水管8,右端连接蠕动泵,使用蠕动泵将氯化钠溶液压入进水管,并通过不断的工作,将经过电解、脱盐后的的氯化钠溶液压入出水管,从而达到海水脱盐的效果,同样将橡皮管插入出水管9,左端插入烧杯中,接取脱盐后的溶液。Working principle: First, fit the
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| CN109264831A (en) * | 2018-11-21 | 2019-01-25 | 江苏科技大学 | Asymmetric capacitor desalination device and method for desalting using the same |
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| CN201165478Y (en) * | 2008-01-18 | 2008-12-17 | 朝阳森塬活性炭有限公司 | Sea water electric desalting apparatus |
| CN102225796A (en) * | 2009-06-16 | 2011-10-26 | 杨国锋 | A flow-type electrolyzed water manufacturing device |
| CN103675054A (en) * | 2012-09-25 | 2014-03-26 | 方建辉 | Electrolytic tank and method for detecting dopamine |
| CN103896339A (en) * | 2012-12-27 | 2014-07-02 | 北京汉能创昱科技有限公司 | Preparation method of sodium manganese oxide |
| CN104897639A (en) * | 2015-05-06 | 2015-09-09 | 同济大学 | In Situ Raman Photoelectrochemical Cell Using TiO2NTs/Ti Sheet Electrode and Its Application |
| JP2015182008A (en) * | 2014-03-24 | 2015-10-22 | 株式会社東芝 | Electrolyzed water generator |
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| CN201165478Y (en) * | 2008-01-18 | 2008-12-17 | 朝阳森塬活性炭有限公司 | Sea water electric desalting apparatus |
| CN102225796A (en) * | 2009-06-16 | 2011-10-26 | 杨国锋 | A flow-type electrolyzed water manufacturing device |
| CN103675054A (en) * | 2012-09-25 | 2014-03-26 | 方建辉 | Electrolytic tank and method for detecting dopamine |
| CN103896339A (en) * | 2012-12-27 | 2014-07-02 | 北京汉能创昱科技有限公司 | Preparation method of sodium manganese oxide |
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