CN202246890U - Membrane polar distance ion membrane electrolysis bath - Google Patents
Membrane polar distance ion membrane electrolysis bath Download PDFInfo
- Publication number
- CN202246890U CN202246890U CN2011203180667U CN201120318066U CN202246890U CN 202246890 U CN202246890 U CN 202246890U CN 2011203180667 U CN2011203180667 U CN 2011203180667U CN 201120318066 U CN201120318066 U CN 201120318066U CN 202246890 U CN202246890 U CN 202246890U
- Authority
- CN
- China
- Prior art keywords
- net
- cathode
- membrane
- edge
- disc
- 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
Links
Images
Classifications
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
Abstract
The utility model relates to a membrane polar distance ion membrane electrolysis bath, which comprises a cathode disc (1) and a cathode net (3) and is characterized in that a nickel plate strip (2) is arranged between the cathode disc (1) and the cathode net (3), an elastic net (4), a covering net (5) and a cathode active net (6) are sequentially arranged on the cathode net (3), the bottom surface of the elastic net (4) is welded with the cathode net (3), the edge of the covering net (5) is welded with the cathode net (3), and the edge of the cathode active net (6) is welded with the edge of the sealing surface of the cathode disc (1) through a nickel belt. The membrane polar distance ion membrane electrolysis bath has the advantages that because the cathode net and an ion membrane are flexibly pasted through the elastic net, the membrane polar distance is realized, and the energy saving effect is reached; and the cathode net is changed into a nickel wire woven net from an original pull-hole net, and the electrolysis specific surface area is increased, so the current distribution is uniform, the bath voltage is dropped, the electrolysis efficiency is improved, and the energy saving effect is obvious.
Description
Technical field
The utility model relates to a kind of ion-exchange membrane electrolyzer, relates in particular to a kind of film pole span ion-exchange membrane electrolyzer, belongs to technical filed of chlor-alkali equipment.
Background technology
Ion-exchange membrane electrolyzer makes the chlorine industry specific equipment, and its effect makes through electrolytic brine and produces caustic soda and chlorine.Chlorine industry is as the highly energy-consuming industry, and save energy is raised the efficiency, and employing new technology energy-saving and cost-reducing with advanced and applicable technology is Eternal Theme.Japan's chlorine engineering BiTAC cell construction is followed successively by anode network, anode disc, cathode disc, spring piece and cathode screen from the bottom up.Phenomenons such as following deficiency is arranged during design: 1, the negative and positive polar net is thickness 1mm sheet material pulling eye net, and the pit that wire side forms because of resistance welding and spring piece elasticity are inhomogeneous make and have only part and ionic membrane applying between the negative and positive polar net, or do not fit, the generation pole span; 2, the conduction point of contact of cathode screen and spring piece is less, and only about 640, the cathodic activity coatingsurface is coarse.Because of spring piece and cathode screen point of contact are few, distribution of current is inhomogeneous, influences the use properties of electrolyzer; So electrolytic bath voltage is high, energy consumption is high, damages ionic membrane easily.
The utility model content
The purpose of the utility model is to overcome above-mentioned deficiency, provides a kind of performance the higher and tangible film pole span of energy-saving effect ion-exchange membrane electrolyzer.
The purpose of the utility model is achieved in that a kind of film pole span ion-exchange membrane electrolyzer; Comprise cathode disc and cathode screen, be provided with the nickel lath between said cathode disc and the cathode screen, be provided with elastic network(s), nerve of a covering and cathodic activity net on the said cathode screen successively; The bottom surface of said elastic network(s) and cathode screen welding; The edge of said nerve of a covering and cathode screen welding, said cathodic activity net adopt thin nickel strap to be welded on the edge of cathode disc trim, and said elastic network(s) is the nickel wire mesh grid; Said activated cathode net is the nickel wire mesh grid, and the surface of said activated cathode net is provided with the heated oxide noble coatings.
Compared with prior art, the beneficial effect of the utility model is:
The utility model has been realized the film pole span owing to fit through elastic network(s) is flexible between cathode screen and ionic membrane, reaches energy-saving effect; Cathode screen has become the nickel wire mesh grid by original pulling eye net, and the electrolysis specific surface area increases, and makes distribution of current even, and bath voltage descends, and electrolytic efficiency improves, and energy-saving effect is remarkable.
Description of drawings
Fig. 1 is the structural representation of the utility model.
Wherein:
Nickel lath 2
Cathode screen 3
Elastic network(s) 4
Active net 5
Cathodic activity net 6.
Embodiment
Referring to Fig. 1, a kind of film pole span ion-exchange membrane electrolyzer that the utility model relates to comprises cathode disc 1 and cathode screen 3, is provided with nickel lath 2 between said cathode disc 1 and the cathode screen 3, is provided with elastic network(s) 4, nerve of a covering 5 and cathodic activity net 6 on the said cathode screen 3 successively.The bottom surface of said elastic network(s) 4 and cathode screen 3 welding, the edge of said nerve of a covering 5 and cathode screen 3 welding, said cathodic activity net 6 adopts thin nickel strap to be welded on the edge of cathode disc 1 trim.Said elastic network(s) 4 is the nickel wire mesh grid, and said activated cathode net 6 is the nickel wire mesh grid, and the surface of said activated cathode net 6 is provided with the heated oxide noble coatings.
Claims (3)
1. film pole span ion-exchange membrane electrolyzer; Comprise cathode disc (1) and cathode screen (3); It is characterized in that being provided with nickel lath (2) between said cathode disc (1) and the cathode screen (3); Be provided with elastic network(s) (4), nerve of a covering (5) and cathodic activity net (6) on the said cathode screen (3) successively; The bottom surface of said elastic network(s) (4) and cathode screen (3) welding, the edge of said nerve of a covering (5) and cathode screen (3) welding, the edge of the edge of said cathodic activity net (6) and cathode disc (1) trim is through the nickel strap welding.
2. a kind of film pole span ion-exchange membrane electrolyzer according to claim 1 is characterized in that said elastic network(s) (4) is the nickel wire net.
3. a kind of film pole span ion-exchange membrane electrolyzer according to claim 1 is characterized in that said activated cathode net (6) is the nickel wire net, and said activated cathode net (6) surface is provided with the heated oxide noble coatings.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203180667U CN202246890U (en) | 2011-08-29 | 2011-08-29 | Membrane polar distance ion membrane electrolysis bath |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN2011203180667U CN202246890U (en) | 2011-08-29 | 2011-08-29 | Membrane polar distance ion membrane electrolysis bath |
Publications (1)
Publication Number | Publication Date |
---|---|
CN202246890U true CN202246890U (en) | 2012-05-30 |
Family
ID=46108160
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN2011203180667U Expired - Fee Related CN202246890U (en) | 2011-08-29 | 2011-08-29 | Membrane polar distance ion membrane electrolysis bath |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN202246890U (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109706474A (en) * | 2019-01-29 | 2019-05-03 | 北京瑞纳旭邦科技有限公司 | Film pole span remodeling method |
CN109706473A (en) * | 2019-01-29 | 2019-05-03 | 北京瑞纳旭邦科技有限公司 | The method of chlorine engineering electricity slot restructuring film pole span |
-
2011
- 2011-08-29 CN CN2011203180667U patent/CN202246890U/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109706474A (en) * | 2019-01-29 | 2019-05-03 | 北京瑞纳旭邦科技有限公司 | Film pole span remodeling method |
CN109706473A (en) * | 2019-01-29 | 2019-05-03 | 北京瑞纳旭邦科技有限公司 | The method of chlorine engineering electricity slot restructuring film pole span |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EA201170697A1 (en) | ELEMENTARY CELL AND RELATED MODULAR ELECTROLYZER FOR ELECTROLYTIC PROCESSES | |
WO2012156671A3 (en) | Electrochemical cell and method for operation of the same | |
CN202246890U (en) | Membrane polar distance ion membrane electrolysis bath | |
CN103388161B (en) | A kind of film electrowinning plant for solution of metal sulfates refining | |
CN102534651A (en) | Electrolytic tank with zero polar distance | |
CN204793034U (en) | Negative pole bars for lead acid battery | |
CN101831665A (en) | Method for improving ion film electrolyser by film polar distance technology | |
CN202094214U (en) | Lead-acid battery electrode plate gird | |
CN201506837U (en) | Membrane polar distance ion membrane electrolytic tank | |
CN203683683U (en) | Improved ionic membrane electrolysis bath | |
CN202492585U (en) | Zero pole electrolytic cell | |
CN203625487U (en) | Zero polar distance ionic membrane electrolyzer | |
CN201665714U (en) | Monopolar type membrane polar-distance electrolytic bath | |
CN207608638U (en) | A kind of foil machine upper liquid hole anode plate | |
CN202072788U (en) | Strip steel electrolyzing and cleaning electrode plate | |
CN202246892U (en) | Single pole type membrane polar distance electrolytic tank | |
CN205556792U (en) | Zero pole span electrolysis trough | |
CN203270045U (en) | Electrolytic cell for producing caustic soda | |
CN203007427U (en) | Ionic membrane electrolysis unit cell | |
CN202658238U (en) | Repolarization ionic membrane electrolyzer membrane pole pitch electrode | |
CN202499914U (en) | Organic synthetic chemical electrolytic tank | |
CN201670884U (en) | Net structural plate electrode of oxyhydrogen energy equipment | |
CN203007435U (en) | Expanding anode arranged in electrolytic tank | |
CN101805909A (en) | Monopolar type membrane polar distance electrolytic bath | |
CN202246926U (en) | Novel electrolysis bath |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120530 Termination date: 20170829 |