CN201793757U - Sodium chlorate electrolytic bath - Google Patents
Sodium chlorate electrolytic bath Download PDFInfo
- Publication number
- CN201793757U CN201793757U CN2010205191619U CN201020519161U CN201793757U CN 201793757 U CN201793757 U CN 201793757U CN 2010205191619 U CN2010205191619 U CN 2010205191619U CN 201020519161 U CN201020519161 U CN 201020519161U CN 201793757 U CN201793757 U CN 201793757U
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- plate
- anode
- titanium
- welding
- end plate
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Abstract
The utility model discloses a sodium chlorate electrolytic bath, which comprises a shell, a cathode assembly and an anode assembly, wherein the anode assembly comprises a conductive connecting plate, an anode end plate and an anode plate; and one end of the conductive connecting plate is connected with the anode end plate by welding, one end of the anode plate is connected with the anode end plate by welding, and the anode end plate is an aluminum-titanium composite plate. In the aluminum-titanium composite plate, a supporting gasket is arranged between an aluminum plate and a titanium plate, and the supporting gasket, the aluminum plate and the titanium plate are connected into a whole by explosive welding, wherein the thickness of the aluminum plate is 10 to 30 millimeters, and the thickness of the titanium plate 2 is 6 to 12 millimeters. The joint rate of the aluminum-titanium composite plate reaches 99 percent, and the shearing strength tau b is more than or equal to 210MPa.
Description
Technical field
The utility model relates to a kind of sodium chlorate electrolyzer, relates in particular to a kind of chlorate electrolyser that is provided with the anode compoboard.。
Background technology
Electrolysis is the key link of production sodium chlorate, the quality of its technical equipment directly influences the cost and the vitality of production of sodium chlorate, the electric energy that the prime cost of electrolysis production sodium chlorate is consumed when being electrolysis, power consumption is little, production cost is just low, thereby just can account in unbeaten row in keen competition market.The consumption that how to reduce electric energy has become to make the gordian technique of electrolyzer producer.Electrolyzer now commonly used is an outer circulation type one pole groove, and it becomes electrolyzer by anode and cathode combination, and anode is made up of conductive connection plates, anode end plate and positive plate.
Because the sodium chlorate product that electrolysis produces is a kind of strong oxidizing property, corrosive Chemicals, so anode end plate and anode strip adopt anticorrosive good titanium material.Consider the electroconductibility of equipment, conductive connection plates adopts aluminium sheet.Conductive connection plates is fixed together by welding and anode end plate, because of contact surface between titanium anode end plate and the aluminium conductive connection plates has the slit, the applying between them is not very desirable, thereby causes electric energy loss because of loose contact in electrolytic process, increase power consumption, increased production cost.Produce the difficult problem that at first must solve that a kind of type material that titanium aluminium can be fit together fully is an electrolyzer manufacturing enterprise, and then improve contact, equipment is cut down the consumption of energy, reduce cost.
Summary of the invention
The purpose of this utility model provides in a kind of electrolytic process that contact is good, and electric energy loss is little, the electrolytic bath electrode plate that production cost reduces.Of the present utility model being achieved by the following technical solution:
A kind of chlorate electrolyser, comprise housing, cathode sets zoarium and anode molectron, wherein the anode molectron comprises conductive connection plates, anode end plate and positive plate, conductive connection plates one end is connected with anode end plate by welding, positive plate one end is connected with anode end plate by welding, and described anode end plate is an aluminium titanium composition board.
Described aluminium titanium composition board is between aluminium sheet and titanium plate support pad to be set, and connects as one by explosive welding.
Described aluminium plate thickness is 10-30 ㎜.
Described titanium plate thickness 6-12 ㎜.
The applying rate of described aluminium titanium composition board reaches 99%.
The shearing resistance τ b 〉=210Mpa of described aluminium titanium composition board.
Adopt aluminium titanium composition board as anode end plate, solved that contact surface has the slit between titanium anode end plate and the aluminium conductive connection plates, the unfavorable problem of fitting, can reduce the electrolysis loss of electrolyzer, cut down the consumption of energy, reduce production costs, reduced the operation of aluminium sheet and titanium plate welding.Lay a good foundation for energy-conservationization of electrolyzer, started the new page of electrolyzer.
Description of drawings
Fig. 1 is the structural representation of aluminium titanium composition board;
Fig. 2 is the structural representation of chlorate electrolyser anode molectron.
Embodiment
As shown in Figure 2, a kind of anode molectron of chlorate electrolyser, wherein the anode molectron comprises conductive connection plates 1, anode end plate 2 and positive plate 3, conductive connection plates 1 one ends are connected with anode end plate 2 by welding, positive plate 3 one ends are connected with anode end plate 2 by welding, and described anode end plate 2 is an aluminium titanium composition board.
As shown in Figure 1, aluminium titanium composition board is to adopt support pad to install between aluminium sheet 1 and titanium plate 3, after the explosive shop is put and is finished, in minor face, arrange the higher explosive of detonation velocity, finally make it to realize large-area continuous combination, connect as one by explosive welding, thickness 10-30 ㎜ of aluminium sheet, titanium plate thickness 6-12 ㎜, aluminium titanium composition board after the explosive welding once shaped has solved that contact surface has the slit between titanium anode end plate and the aluminium conductive connection plates, the unfavorable problem of fitting, aluminium titanium composition board by explosive welding can make the applying rate reach more than 99%, minimum shearing resistance τ b 〉=210Mpa.
Claims (6)
1. chlorate electrolyser, comprise housing, cathode sets zoarium and anode molectron, wherein the anode molectron comprises conductive connection plates, anode end plate and positive plate, it is characterized in that: conductive connection plates one end is connected with anode end plate by welding, positive plate one end is connected with anode end plate by welding, and described anode end plate is an aluminium titanium composition board.
2. a kind of chlorate electrolyser according to claim 1 is characterized in that: described aluminium titanium composition board is between aluminium sheet and titanium plate support pad to be set, and connects as one by explosive welding.
3. a kind of chlorate electrolyser according to claim 2 is characterized in that: described aluminium plate thickness is 10-30 ㎜.
4. a kind of chlorate electrolyser according to claim 2 is characterized in that: described titanium plate thickness 6-12 ㎜.
5. a kind of chlorate electrolyser according to claim 2 is characterized in that: the applying rate of described aluminium titanium composition board reaches 99%.
6. a kind of chlorate electrolyser according to claim 2 is characterized in that: the shearing resistance τ b 〉=210Mpa of described aluminium titanium composition board.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205191619U CN201793757U (en) | 2010-09-07 | 2010-09-07 | Sodium chlorate electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010205191619U CN201793757U (en) | 2010-09-07 | 2010-09-07 | Sodium chlorate electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201793757U true CN201793757U (en) | 2011-04-13 |
Family
ID=43848677
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010205191619U Expired - Fee Related CN201793757U (en) | 2010-09-07 | 2010-09-07 | Sodium chlorate electrolytic bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201793757U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101942671A (en) * | 2010-09-07 | 2011-01-12 | 苏州卓群钛镍设备有限公司 | Sodium chlorate electrolysis bath |
| WO2015000462A1 (en) * | 2013-07-03 | 2015-01-08 | Vm-Tecsystems Gmbh | Method for treating wastewater and device for carrying out said method |
-
2010
- 2010-09-07 CN CN2010205191619U patent/CN201793757U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101942671A (en) * | 2010-09-07 | 2011-01-12 | 苏州卓群钛镍设备有限公司 | Sodium chlorate electrolysis bath |
| WO2015000462A1 (en) * | 2013-07-03 | 2015-01-08 | Vm-Tecsystems Gmbh | Method for treating wastewater and device for carrying out said method |
| CN105263867A (en) * | 2013-07-03 | 2016-01-20 | Vm-泰克***有限责任公司 | Method for treating wastewater and device for carrying out said method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110413 Termination date: 20120907 |