CN105063659A - Electrolyzer - Google Patents
Electrolyzer Download PDFInfo
- Publication number
- CN105063659A CN105063659A CN201510586676.8A CN201510586676A CN105063659A CN 105063659 A CN105063659 A CN 105063659A CN 201510586676 A CN201510586676 A CN 201510586676A CN 105063659 A CN105063659 A CN 105063659A
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- Prior art keywords
- anode
- negative electrode
- ionic membrane
- electrode
- rubber pad
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Water Treatment By Electricity Or Magnetism (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
Abstract
The invention discloses an electrolyzer. The electrolyzer comprises a tank body (1) and an electrode group (2) which is arranged on the tank body (1); the electrolyzer is characterized in that the electrode group (2) comprises an anode (3) which is connected with a positive electrode of a direct-current power supply and a cathode (4) which is connected with a negative electrode of the direct-current power supply; the anode (3) is a mesh electrode coated with ti-based ruthenium oxide and iridium oxide; the cathode (4) is a titanium mesh electrode; the space between the anode (3) and the cathode (4) is divided into an anode chamber and a cathode chamber by adopting an ionic membrane (5); the anode (3) and the ionic membrane (5) as well as the ionic membrane (5) and the cathode (4) are fixed through PVC (Poly Vinyl Chloride) plate grids (6); strongly alkaline water can flow out after tap water entering from a water inlet pipe is electrolyzed by the cathode chamber. According to the electrolyzer disclosed by the invention, the alkalinity of the tap water can be rapidly increased within unit time, the electrolytic efficiency is increased, and the power consumption is reduced.
Description
Technical field
The present invention relates to electrolyzer Application Areas, particularly relate to the electrolyzer that a kind of electrolysis strong lye removes organophosphorus pesticide.
Background technology
Electrolyzed functional water is also known as electric potential water, brine electrolysis or ionized water, it to refer to ionogen dilute solution in special device through electric field treatment, the indexs such as the pH value of water, redox potential (ORP value), residual chlorine concentrations are changed and produce there is the acid electrolyzed functional water of specific function and the general name of alkaline ion water, according to the characteristic of Electricity Functional Water, the rapid decomposable organophosphorus pesticide of electrolysis strong lye.
At present, electrolyzer of the prior art, the speed of its quick electrolysis tap water alkalescence is slow, can not meet high efficiency electrolysis work in factory.
Summary of the invention
For overcoming above-mentioned shortcoming, the object of the present invention is to provide a kind of electrolyzer, having reached the alkalescence improving rapidly tap water in the unit time, improve electrolytic efficiency, reach the object of saving energy.
In order to reach above object, the technical solution used in the present invention is: a kind of electrolyzer, the electrode group comprising cell body and arrange thereon, described electrode group comprises the anode be connected with DC power anode and the negative electrode be connected with DC power cathode, described anode is titanium base ruthenium oxide and iridium oxide coated mesh electrode, described negative electrode is titanium net electrode, ionic membrane is adopted to be divided into anolyte compartment and cathode compartment between described anode and negative electrode, fixed by PVC board grid between described anode and ionic membrane and between ionic membrane and negative electrode, the tap water that water inlet pipe enters by described cathode compartment can flow out strong alkaline water after electrolysis.This electrolyzer is put into PVC tank, the tap water entered by water inlet pipe by cathode compartment can flow out strong alkaline water fast after electrolysis, groove is removed again to putting into residue of pesticide in it, soak several minutes and just can remove residue of pesticide fast, anode is titanium base ruthenium oxide and iridium oxide coated mesh electrode, negative electrode is titanium net, and electrode is fixed by PVC board grid due to anode and negative electrode, and also adopt ionic membrane to be divided into anolyte compartment and cathode compartment therebetween, it is made to improve the alkalescence of tap water electrolysis fast in the unit time, and then raising electrolytic efficiency, reach the object of saving energy.
Further, the pvc pipe being all inserted in regular length by CARBURIZING FURNACE FOR STAINLESS FASTENER between described anode, ionic membrane and negative electrode and PVC board grid is fixed.By CARBURIZING FURNACE FOR STAINLESS FASTENER fixedly make between anode, ionic membrane and negative electrode and PVC board grid more solid and reliable, avoid its produce produce displacement.
Further, soft rubber pad is all adopted to seal between described anode, ionic membrane and negative electrode and PVC board grid.Soft rubber pad not only plays the effect of sealing, also can more promote its electrolytic efficiency.
Further, its assembling mode is followed successively by negative electrode, soft rubber pad, PVC board grid, soft rubber pad, ionic membrane, soft rubber pad, PVC board grid, soft rubber pad, anode, soft rubber pad.This assembling mode can play effective fixing, effectively seal, and the more effective alkalescence improving tap water electrolysis fast, and then improve electrolytic efficiency.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present embodiment;
Fig. 2 is the packaging assembly schematic diagram of the electrode group of the present embodiment.
In figure:
1-cell body; 2-electrode group; 3-anode; 4-negative electrode; 5-ionic membrane; 6-PVC grid; 7-soft rubber pad.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present invention is described in detail, can be easier to make advantages and features of the invention be readily appreciated by one skilled in the art, thus more explicit defining is made to protection scope of the present invention.
Shown in accompanying drawing 1-2, a kind of electrolyzer of the present embodiment, the electrode group 2 comprising cell body 1 and arrange thereon, electrode group 2 comprises the anode 3 be connected with DC power anode and the negative electrode 4 be connected with DC power cathode, anode 3 is titanium base ruthenium oxide and iridium oxide coated mesh electrode, negative electrode 4 is titanium net electrode, ionic membrane 5 is adopted to be divided into anolyte compartment and cathode compartment between anode 3 and negative electrode 4, fixed by PVC board grid 6 between anode 3 and ionic membrane 5 and between ionic membrane 5 and negative electrode 4, anode 3, ionic membrane 5 and the pvc pipe being all inserted in regular length by CARBURIZING FURNACE FOR STAINLESS FASTENER between negative electrode 4 and PVC board grid 6 are fixed, anode 3, ionic membrane 5 and all adopt soft rubber pad 7 to seal between negative electrode 4 and PVC board grid 6, its assembling mode is followed successively by negative electrode 4, soft rubber pad 7, PVC board grid 6, soft rubber pad 7, ionic membrane 5, soft rubber pad 7, PVC board grid 6, soft rubber pad 7, anode 3, soft rubber pad 7, the tap water that water inlet pipe enters by cathode compartment can flow out strong alkaline water after electrolysis, be immersed in strong alkaline water by residue of pesticide being removed groove, several minutes just can remove residue of pesticide fast.
Above embodiment is only for illustrating technical conceive of the present invention and feature; its object is to allow person skilled in the art understand content of the present invention and to be implemented; can not limit the scope of the invention with this; all equivalences done according to spirit of the present invention change or modify, and all should be encompassed in protection scope of the present invention.
Claims (4)
1. an electrolyzer, the electrode group (2) comprising cell body (1) and arrange thereon, it is characterized in that: described electrode group (2) comprises the anode (3) be connected with DC power anode and the negative electrode (4) be connected with DC power cathode, described anode (3) is titanium base ruthenium oxide and iridium oxide coated mesh electrode, described negative electrode (4) is titanium net electrode, ionic membrane (5) is adopted to be divided into anolyte compartment and cathode compartment between described anode (3) and negative electrode (4), fixed by PVC board grid (6) between described anode (3) and ionic membrane (5) and between ionic membrane (5) and negative electrode (4), the tap water that water inlet pipe enters by described cathode compartment can flow out strong alkaline water after electrolysis.
2. a kind of electrolyzer according to claim 1, is characterized in that: described anode (3), ionic membrane (5) and the pvc pipe being all inserted in regular length by CARBURIZING FURNACE FOR STAINLESS FASTENER between negative electrode (4) and PVC board grid (6) are fixed.
3. a kind of electrolyzer according to claim 2, is characterized in that: described anode (3), ionic membrane (5) and all adopt soft rubber pad to seal (7) between negative electrode (4) and PVC board grid (6).
4. a kind of electrolyzer according to claim 3, is characterized in that: its assembling mode is followed successively by negative electrode (4), soft rubber pad (7), PVC board grid (6), soft rubber pad (7), ionic membrane (5), soft rubber pad (7), PVC board grid (6), soft rubber pad (7), anode (3), soft rubber pad (7).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510586676.8A CN105063659B (en) | 2015-09-15 | 2015-09-15 | A kind of electrolysis unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510586676.8A CN105063659B (en) | 2015-09-15 | 2015-09-15 | A kind of electrolysis unit |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105063659A true CN105063659A (en) | 2015-11-18 |
| CN105063659B CN105063659B (en) | 2018-05-08 |
Family
ID=54493155
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510586676.8A Active CN105063659B (en) | 2015-09-15 | 2015-09-15 | A kind of electrolysis unit |
Country Status (1)
| Country | Link |
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| CN (1) | CN105063659B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107265571A (en) * | 2017-06-05 | 2017-10-20 | 王雪霏 | The retracting device of alkali and acid group |
| CN110603231A (en) * | 2017-05-09 | 2019-12-20 | 松下知识产权经营株式会社 | Electrolyzed water generation device |
Citations (9)
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| CN1132115A (en) * | 1994-12-06 | 1996-10-02 | 罗纳·布朗克纤维和树脂中间体公司 | Galvano-chemistry prepn. method of catalyst on basis of transition metal and phosphine |
| US6187169B1 (en) * | 1996-09-16 | 2001-02-13 | Atofina Chemicals, Inc. | Generation of organosulfonic acid from its salts |
| CN1435512A (en) * | 2002-01-30 | 2003-08-13 | 友昕科技股份有限公司 | Ozone producing electrolyzer |
| CN1453395A (en) * | 2002-04-25 | 2003-11-05 | 北京有色金属研究总院 | Electrolytic reduction process of preparing bivalent europium |
| CN2623701Y (en) * | 2003-03-13 | 2004-07-07 | 铁岭科拓橡塑有限责任公司 | Lonic membrane electrolytic bath rubber sheet gasket |
| CN102877085A (en) * | 2012-09-24 | 2013-01-16 | 山东东岳高分子材料有限公司 | Method for preparing high-purity peroxysulphate based on electrolytic oxidation through ion-exchange membrane electrolyzer for chlor-alkali production |
| CN103014778A (en) * | 2012-12-11 | 2013-04-03 | 北京矿冶研究总院 | Ore pulp electrolysis device |
| CN203999837U (en) * | 2014-06-27 | 2014-12-10 | 四川省银河化学股份有限公司 | Novel electrolytic bath |
| CN204999982U (en) * | 2015-09-15 | 2016-01-27 | 苏州市铂瑞工业材料科技有限公司 | Electrolysis unit |
-
2015
- 2015-09-15 CN CN201510586676.8A patent/CN105063659B/en active Active
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|---|---|---|---|---|
| CN1132115A (en) * | 1994-12-06 | 1996-10-02 | 罗纳·布朗克纤维和树脂中间体公司 | Galvano-chemistry prepn. method of catalyst on basis of transition metal and phosphine |
| US6187169B1 (en) * | 1996-09-16 | 2001-02-13 | Atofina Chemicals, Inc. | Generation of organosulfonic acid from its salts |
| CN1435512A (en) * | 2002-01-30 | 2003-08-13 | 友昕科技股份有限公司 | Ozone producing electrolyzer |
| CN1453395A (en) * | 2002-04-25 | 2003-11-05 | 北京有色金属研究总院 | Electrolytic reduction process of preparing bivalent europium |
| CN2623701Y (en) * | 2003-03-13 | 2004-07-07 | 铁岭科拓橡塑有限责任公司 | Lonic membrane electrolytic bath rubber sheet gasket |
| CN102877085A (en) * | 2012-09-24 | 2013-01-16 | 山东东岳高分子材料有限公司 | Method for preparing high-purity peroxysulphate based on electrolytic oxidation through ion-exchange membrane electrolyzer for chlor-alkali production |
| CN103014778A (en) * | 2012-12-11 | 2013-04-03 | 北京矿冶研究总院 | Ore pulp electrolysis device |
| CN203999837U (en) * | 2014-06-27 | 2014-12-10 | 四川省银河化学股份有限公司 | Novel electrolytic bath |
| CN204999982U (en) * | 2015-09-15 | 2016-01-27 | 苏州市铂瑞工业材料科技有限公司 | Electrolysis unit |
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| 哈曼等: "《电化学》", 31 January 2010, 化学工业出版社 * |
| 王世荣: "隔膜法电解工序防腐蚀措施探讨", 《氯碱工业》 * |
| 聂巨亮: "离子膜电解工艺", 《河北化工》 * |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110603231A (en) * | 2017-05-09 | 2019-12-20 | 松下知识产权经营株式会社 | Electrolyzed water generation device |
| CN107265571A (en) * | 2017-06-05 | 2017-10-20 | 王雪霏 | The retracting device of alkali and acid group |
| CN107265571B (en) * | 2017-06-05 | 2024-02-27 | 王雪霏 | Alkali and acid radical recovery device |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105063659B (en) | 2018-05-08 |
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| C06 | Publication | ||
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| CB02 | Change of applicant information | ||
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Address after: Golden Bridge Industrial Park, Wuzhong District Mudu town of Suzhou city in Jiangsu province 215100 No. 51 Industrial Zone No. 4 Applicant after: Suzhou platinum electrode Industrial Co., Ltd. Address before: Golden Bridge Industrial Park, Wuzhong District Mudu town of Suzhou city in Jiangsu province 215100 No. 51 Industrial Zone No. 4 Applicant before: SUZHOU BORUI INDUSTRIAL MATERIAL TECHNOLOGY CO., LTD. |
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Address after: 215131 No. 6225 Guangji North Road, Beiqiao Street, Xiangcheng District, Suzhou City, Jiangsu Province Patentee after: Suzhou platinum electrode Industrial Co., Ltd. Address before: Golden Bridge Industrial Park, Wuzhong District Mudu town of Suzhou city in Jiangsu province 215100 No. 51 Industrial Zone No. 4 Patentee before: Suzhou platinum electrode Industrial Co., Ltd. |