CN2195552Y - Electrolysis bath for processing metal manganese - Google Patents
Electrolysis bath for processing metal manganese Download PDFInfo
- Publication number
- CN2195552Y CN2195552Y CN 94237549 CN94237549U CN2195552Y CN 2195552 Y CN2195552 Y CN 2195552Y CN 94237549 CN94237549 CN 94237549 CN 94237549 U CN94237549 U CN 94237549U CN 2195552 Y CN2195552 Y CN 2195552Y
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- CN
- China
- Prior art keywords
- electrolyzer
- diaphragm frame
- utility
- model
- metal manganese
- 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
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to an improved electrolysis tank for metal manganese. The homopolar spacing of the electrolysis tank is shortened to 80 mm, and the voltage of the electrolysis tank is decreased to 4.2V under the condition of unchanging current intensity. In addition, an electrolysis false bottom and a septum frame are changed to be made of PVC plastic, and sheet-shaped septum cloth is changed to sleeve type barrel cloth at the same time. Thus, the utility model has the characteristics of good acid resistance, high strength, small size, less electricity consumption, etc.
Description
The utility model relates to a kind of electrolytic metal Mn production-scale cell, is improvements over the prior art.
The existing electrolyzer that is used for manganese metal production, its diaphragm frame, the false end, are ligneous, and its acid resistance is poor, intensity is low, is difficult to satisfy meticulousr processing request, and its diaphragm cloth is that sheet is made and formed, be difficult to reach unified requirement of tightening, influence is determined with interpole gap; And since bigger with interpole gap, make bath voltage too high, and power consumption is bigger.
The purpose of this utility model provides a kind of under the constant situation of strength of current, changes electrolyzer portion parts material and same interpole gap, reduces the electrolyzer of bath voltage.
The utility model is improvements over the prior art.It by 100 original～110mm, foreshortens to 76 present～84mm with the spacing between the homopolarity in the electrolyzer, and the hypotelorism to 38 between the different poles～42mm makes bath voltage drop to 4～4.2V by original 5V; In addition,, change the false end of electrolyzer and diaphragm frame into the PVC plastic production by original wood materials, simultaneously plate diaphragm cloth is made the diaphragm frame cloth bag and change a cloth into, be convenient to process and tighten in order to satisfy the processing requirement of above-mentioned shortening spacing.
The utility model after the improvement, it is good to have an acid resistance, and intensity is big, and volume is little, and bath voltage is low, characteristics such as little power consumption.
Fig. 1 is the cell construction synoptic diagram.
Fig. 2 is a diaphragm frame cloth bag synoptic diagram.
Fig. 3 is the electrolyzer vertical view.
1, electrolyzer anchor 2, cell body 3, liner 4, anode diaphragm frame
5, diaphragm frame cloth bag 6, the false end 7 of electrolyzer, false end sealing frame
8, false underframe 9, pressing plate 10, cooling tube
11, sewage draining exit 12, positive plate 13, negative plate
The utility model is described in further detail below in conjunction with accompanying drawing.
As Fig. 1, shown in Figure 3, electrolyzer of the present utility model is on the basis of existing technology, spacing between the homopolarity (13 of 12 of positive plates or negative plates) is foreshortened to present 80mm by original 100mm, hypotelorism between positive plate 12 and the negative plate 13 is to 40mm, under the constant situation of strength of current, make voltage drop to 4V by original 5V.In addition, in order to satisfy the processing requirement of above-mentioned shortening, use the false end 6 of electrolyzer and anode diaphragm frame 4 instead the PVC plastic production with interpole gap; To make diaphragm frame cloth bag 5 by plate diaphragm cloth simultaneously, change tube cloth as shown in Figure 2 into, and be convenient to process and tighten.
The utility model after the improvement, its acid resistance is good, the frame strength height, volume is little.And, make electric energy efficiency bring up to 0.4235 by 0.357 because shortening has reduced bath voltage with interpole gap, therefore, can reduce on original basis more than the power consumption 1000Kwh/ ton manganese.
Claims (3)
1, a kind of improved metal manganese electrolytic bath of producing is made of anchor, cell body, diaphragm frame, diaphragm frame cloth bag, positive plate, negative plate, the false end, pressing plate etc., it is characterized in that:
A, homopolarity hypotelorism are 76～84mm, and the different poles spacing is 38～42mm;
B, the false end of electrolyzer and diaphragm frame are the PVC plastics;
2, electrolyzer according to claim 1, it is characterized in that best is 80mm with interpole gap, the different poles spacing is 40mm.
3, electrolyzer according to claim 1 and 2 is characterized in that the diaphragm frame cloth bag is the cartridge type woven dacron.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94237549 CN2195552Y (en) | 1994-06-08 | 1994-06-08 | Electrolysis bath for processing metal manganese |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 94237549 CN2195552Y (en) | 1994-06-08 | 1994-06-08 | Electrolysis bath for processing metal manganese |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN2195552Y true CN2195552Y (en) | 1995-04-26 |
Family
ID=33845212
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 94237549 Expired - Fee Related CN2195552Y (en) | 1994-06-08 | 1994-06-08 | Electrolysis bath for processing metal manganese |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN2195552Y (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101307463B (en) * | 2008-07-16 | 2010-06-02 | 中信锦州铁合金股份有限公司 | Method for producing electrolytic manganese metal by replacing partial ammonia water with manganese dregs for neutralization deironing |
| CN102296323A (en) * | 2010-06-22 | 2011-12-28 | 陈榜龙 | Manufacturing system for producing electrolytic manganese metal by two-ore method |
-
1994
- 1994-06-08 CN CN 94237549 patent/CN2195552Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101307463B (en) * | 2008-07-16 | 2010-06-02 | 中信锦州铁合金股份有限公司 | Method for producing electrolytic manganese metal by replacing partial ammonia water with manganese dregs for neutralization deironing |
| CN102296323A (en) * | 2010-06-22 | 2011-12-28 | 陈榜龙 | Manufacturing system for producing electrolytic manganese metal by two-ore method |
| WO2011160575A1 (en) * | 2010-06-22 | 2011-12-29 | Chen Banglong | Manufacturing system for producing electrolytic manganese metal by two-mining method |
| CN102296323B (en) * | 2010-06-22 | 2014-11-05 | 陈榜龙 | Manufacturing system for producing electrolytic manganese metal by two-ore method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |