CN202968214U - Electrolytic water tank - Google Patents

Electrolytic water tank Download PDF

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Publication number
CN202968214U
CN202968214U CN 201220694265 CN201220694265U CN202968214U CN 202968214 U CN202968214 U CN 202968214U CN 201220694265 CN201220694265 CN 201220694265 CN 201220694265 U CN201220694265 U CN 201220694265U CN 202968214 U CN202968214 U CN 202968214U
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CN
China
Prior art keywords
water
electrolytic
electrode pipe
anode electrode
water outlet
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN 201220694265
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Chinese (zh)
Inventor
王辉明
喻辉
张竞
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
ANHUI YUSHI TECHNOLOGY Co Ltd
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ANHUI YUSHI TECHNOLOGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ANHUI YUSHI TECHNOLOGY Co Ltd filed Critical ANHUI YUSHI TECHNOLOGY Co Ltd
Priority to CN 201220694265 priority Critical patent/CN202968214U/en
Application granted granted Critical
Publication of CN202968214U publication Critical patent/CN202968214U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model discloses an electrolytic water tank, comprising an electrolytic tank body, a water inlet, an alkaline water outlet and an acidulous water outlet, wherein the alkaline water outlet and the acidulous water outlet are formed in the electrolytic tank body; the water inlet is connected with the electrolytic water tank through a back-flushing reversing valve; the electrolytic tank body comprises a shell, a cathode electrode tube, an anode electrode tube and a tubular ultrafiltration membrane; the cathode electrode tube is connected to the inner wall of the shell; the ultrafiltration membrane is sleeved outside the anode electrode tube; and a gap is formed between the inner wall of the ultrafiltration membrane and the outer wall of the anode electrode tube. By adopting the structure, the electrolytic water tank has the advantages that the electrolytic water tank occupies small area, the installation is facilitated, the effective working area of electrodes is improved, the generation amount of acidic electrolytic water is greatly reduced, and meanwhile, the voltage required by an electrolysis polar plate is greatly reduced, and the pH value adjustment sensitivity of the generated electrolytic water is greatly improved.

Description

A kind of electrolysis water trough
Technical field
The utility model relates to the brine electrolysis technical field, particularly a kind of electrolysis water trough.
Background technology
Brine electrolysis is present advanced country in the world acknowledged safety, state-of-the-art water, is also unique water that meets the World Health Organization's " large standard of good water six " fully.It is take tap water as raw material, and tap water is by electrolyzed water machine the time, and water is functionalized in electrolytic process.The brine electrolysis industry appears on the market so far, has obtained very big development on Europe, the United States, Japan and Korea S., platform and South East Asia and other places.Over past ten years, along with the enhancing of China's national health consciousness, also more and more higher to the requirement of drinking water quality, and the health care curative effect concept of drinking brine electrolysis, obtain successively the numerous common people's confirmation, various family expenses electrolysis water dispensers also progressively become the essential equipment of family.The electrolyzer assembly that family expenses electrolysis water dispenser in the market adopts basically is all flat electrolyzers, although it is little to have occupation of land, the advantage such as easy for installation, but it is little to exist the effective working area of electrode, the brine electrolysis lack of homogeneity, the shortcomings such as made sour water and the basic equivalent of alkaline water.Therefore how to improve electrolytic efficiency and its homogeneity of electrode plate of electrolytic tank, the growing amount that makes it reduction sour water in the electrolyzed alkaline water that generation is drunk is the problem that prior art need to solve.
The utility model content
Technical problem to be solved in the utility model is for the deficiencies in the prior art, to provide a kind of electrolysis water trough that growing amount little, easy for installation, that make acidic electrolytic water greatly reduces, the potential of hydrogen of the brine electrolysis that generates adjusting sensitivity significantly improves that takes up an area.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of electrolysis water trough, comprise cell body, water-in, be arranged on alkaline water water outlet and sour water water outlet on cell body, described water-in is connected with cell body by Backflush reversing valve, described cell body comprises the ultra-filtration membrane of housing, cathode electrode pipe, anode electrode pipe, tubulose, described cathode electrode pipe is connected on inner walls, described ultra-filtration membrane is enclosed within outside the anode electrode pipe, is provided with the gap between the outer wall of the inwall of ultra-filtration membrane and anode electrode pipe.
Described cathode electrode pipe is connected with described alkaline water water outlet with cavity between ultra-filtration membrane, is connected in described sour water water outlet and anode electrode pipe.
The tube wall of described anode electrode pipe is netted.
Described cell body is fixed on support.
Described housing adopts the PPR material.
Described cathode electrode pipe, anode electrode pipe are titanium alloy electrode.
The utility model adopts said structure, has the following advantages: 1, not only have and take up an area little, easy for installation original advantage, also improved effective working area of electrode; 2, the growing amount of acidic electrolytic water is greatly reduced.Simultaneously, voltage required on electrolytic pole board is reduced greatly, the potential of hydrogen of the brine electrolysis that generates is regulated sensitivity and is significantly improved.
Description of drawings
Below in conjunction with the drawings and specific embodiments, the utility model is described in further detail;
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of electrolyzer in the utility model;
In Fig. 1 ~ Fig. 2,1, water-in; 2, alkaline water water outlet; 3, sour water water outlet; 4, Backflush reversing valve; 5, housing; 6, cathode electrode pipe; 7, anode electrode pipe; 8, ultra-filtration membrane; 9, support; 10, power interface.
Embodiment
As Fig. 1 ~ a kind of electrolysis water trough shown in Figure 2, comprise cell body, water-in 1, be arranged on alkaline water water outlet 2 and sour water water outlet 3 on cell body, water-in 1 is connected with cell body by Backflush reversing valve 4, water-in 1 is made by the PPR material, the PPR material is the atactic copolymerized polypropene material, be the quality matetrial of making various water power tubing, performance is better than the PVC material.Water-in 1 connects the tap water through preposition filtration, Backflush reversing valve makes the polarity of electrode paraphase according to the timed interval that sets under the effect of pilot circuit, former negative electrode one end is changed in water inlet flowed into and supercharging, ultra-filtration membrane 8 is carried out counterflush, eliminate its dirt settling.
Cell body comprises the ultra-filtration membrane 8 of housing 5, cathode electrode pipe 6, anode electrode pipe 7, tubulose, and cathode electrode pipe 6 is connected on housing 5 inwalls, and ultra-filtration membrane 8 is enclosed within outside the anode electrode pipe, is provided with the gap between the outer wall of the inwall of ultra-filtration membrane 8 and anode electrode pipe 7.
Cathode electrode pipe 6 is connected with described alkaline water water outlet 2 with cavity between ultra-filtration membrane 8, is connected in sour water water outlet 3 and anode electrode pipe 7.The tube wall of anode electrode pipe 7 is netted.Cell body is fixed on support 9.Housing adopts the PPR material, has electrical isolation, corrosion-resistant, shock resistance.Cathode electrode pipe 6, anode electrode pipe 7 are titanium alloy electrode, non-corrosive.Housing is provided with power interface 10, provides power supply by this power interface to electrolyzer and Backflush reversing valve 4.The shell of support and electrolyzer integrated injection moulding simultaneously is shaped.
Ultra-filtration membrane 8 is nano level aperture filtration membrane, the cationic water (alkalescence) of subset is flowed to the negative potential direction by it, and the anion water of macromolecular mass (acidity) is stayed near positive electrode.The anion water of macromolecular mass is adsorbed by the anode electrode pipe, forms sour water and flows out from the sour water water outlet, and the cationic water of subset is adsorbed by the cathode electrode pipe, forms alkaline water and flows out from the alkaline water water outlet, makes the brine electrolysis that needs.
Electrolysis water trough not only has little, the easy for installation original advantage of occupation of land, has also improved effective working area of electrode, and the growing amount of acidic electrolytic water is greatly reduced.Voltage required on the utility model electrolytic pole board reduces greatly, and the potential of hydrogen of the brine electrolysis that generates is regulated sensitivity and significantly improved.
The above is exemplarily described the utility model by reference to the accompanying drawings; obviously the utility model specific implementation is not subject to the restrictions described above; as long as the various improvement of having adopted method design of the present utility model and technical scheme to carry out; or directly apply to other occasion without improvement, all within protection domain of the present utility model.

Claims (6)

1. electrolysis water trough, it is characterized in that: comprise cell body, water-in (1), be arranged on alkaline water water outlet (2) and sour water water outlet (3) on cell body, described water-in (1) is connected with cell body by Backflush reversing valve (4), described cell body comprises housing (5), cathode electrode pipe (6), anode electrode pipe (7), the ultra-filtration membrane of tubulose (8), described cathode electrode pipe (6) is connected on housing (5) inwall, described ultra-filtration membrane (8) is enclosed within outside the anode electrode pipe, be provided with the gap between the outer wall of the inwall of ultra-filtration membrane (8) and anode electrode pipe (7).
2. a kind of electrolysis water trough according to claim 1, it is characterized in that: described cathode electrode pipe (6) is connected with described alkaline water water outlet (2) with cavity between ultra-filtration membrane (8), is connected in described sour water water outlet (3) and anode electrode pipe (7).
3. a kind of electrolysis water trough according to claim 1, it is characterized in that: the tube wall of described anode electrode pipe (7) is netted.
4. a kind of electrolysis water trough according to claim 1, it is characterized in that: described cell body is fixed on support (9).
5. a kind of electrolysis water trough according to claim 1, is characterized in that: described housing (5) employing PPR material.
6. a kind of electrolysis water trough according to claim 1, it is characterized in that: described cathode electrode pipe (6), anode electrode pipe (7) are titanium alloy electrode.
CN 201220694265 2012-12-15 2012-12-15 Electrolytic water tank Expired - Fee Related CN202968214U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220694265 CN202968214U (en) 2012-12-15 2012-12-15 Electrolytic water tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220694265 CN202968214U (en) 2012-12-15 2012-12-15 Electrolytic water tank

Publications (1)

Publication Number Publication Date
CN202968214U true CN202968214U (en) 2013-06-05

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Family Applications (1)

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CN 201220694265 Expired - Fee Related CN202968214U (en) 2012-12-15 2012-12-15 Electrolytic water tank

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CN (1) CN202968214U (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015154707A1 (en) * 2014-04-12 2015-10-15 大连双迪科技股份有限公司 Health water dispenser
WO2015154708A1 (en) * 2014-04-12 2015-10-15 大连双迪科技股份有限公司 Water electrolysis cup
CN105692731A (en) * 2016-03-16 2016-06-22 武汉大学 Method for treating wastewater with conductive filter material and achieving regeneration
WO2016095229A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and ph adjustment device therefor
CN106587283A (en) * 2016-12-15 2017-04-26 中建水务(深圳)有限公司 Filter and control method
CN110799674A (en) * 2017-04-24 2020-02-14 赫勒电解公司 Method for operating a water electrolysis installation

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015154707A1 (en) * 2014-04-12 2015-10-15 大连双迪科技股份有限公司 Health water dispenser
WO2015154708A1 (en) * 2014-04-12 2015-10-15 大连双迪科技股份有限公司 Water electrolysis cup
WO2016095229A1 (en) * 2014-12-19 2016-06-23 深圳市同盛绿色科技有限公司 Water treatment system and ph adjustment device therefor
CN105692731A (en) * 2016-03-16 2016-06-22 武汉大学 Method for treating wastewater with conductive filter material and achieving regeneration
CN105692731B (en) * 2016-03-16 2019-03-15 武汉大学 It is a kind of that waste water and regeneration method are handled using electric conductivity filtering material
CN106587283A (en) * 2016-12-15 2017-04-26 中建水务(深圳)有限公司 Filter and control method
CN110799674A (en) * 2017-04-24 2020-02-14 赫勒电解公司 Method for operating a water electrolysis installation
CN110799674B (en) * 2017-04-24 2022-05-27 赫勒电解公司 Method for operating a water electrolysis installation
US11371153B2 (en) 2017-04-24 2022-06-28 Hoeller Electrolyzer Gmbh Method for operating a water electrolysis device

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GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20130605

Termination date: 20131215