CN203593795U - Manganese electrolysis bath - Google Patents
Manganese electrolysis bath Download PDFInfo
- Publication number
- CN203593795U CN203593795U CN201320708757.7U CN201320708757U CN203593795U CN 203593795 U CN203593795 U CN 203593795U CN 201320708757 U CN201320708757 U CN 201320708757U CN 203593795 U CN203593795 U CN 203593795U
- Authority
- CN
- China
- Prior art keywords
- bath
- cell body
- slag
- electrolyzer
- anode
- 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 - Lifetime
Links
- 239000011572 manganese Substances 0.000 title claims abstract description 11
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 title claims abstract description 10
- 229910052748 manganese Inorganic materials 0.000 title claims abstract description 10
- 238000005868 electrolysis reaction Methods 0.000 title abstract 5
- 239000004743 Polypropylene Substances 0.000 claims abstract description 5
- -1 polypropylene Polymers 0.000 claims abstract description 5
- 229920001155 polypropylene Polymers 0.000 claims abstract description 5
- 210000005056 cell body Anatomy 0.000 claims description 19
- 239000000463 material Substances 0.000 claims description 8
- 210000004027 cell Anatomy 0.000 claims description 5
- 229920000642 polymer Polymers 0.000 claims description 4
- 239000002893 slag Substances 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 3
- 230000002265 prevention Effects 0.000 abstract 2
- 238000004140 cleaning Methods 0.000 abstract 1
- 238000005260 corrosion Methods 0.000 abstract 1
- 230000007797 corrosion Effects 0.000 abstract 1
- 229920002521 macromolecule Polymers 0.000 abstract 1
- 230000003628 erosive effect Effects 0.000 description 3
- 238000009413 insulation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 238000007654 immersion Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229940074869 marquis Drugs 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002574 poison Substances 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- VBUNOIXRZNJNAD-UHFFFAOYSA-N ponazuril Chemical compound CC1=CC(N2C(N(C)C(=O)NC2=O)=O)=CC=C1OC1=CC=C(S(=O)(=O)C(F)(F)F)C=C1 VBUNOIXRZNJNAD-UHFFFAOYSA-N 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000011150 reinforced concrete Substances 0.000 description 1
- 238000001175 rotational moulding Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 231100000167 toxic agent Toxicity 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Images
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model discloses a manganese electrolysis bath which comprises a bath body (8), a diaphragm frame (1), a false bottom frame and false bottom (7) and an anode liquor chamber (6), wherein an anode liquor overflow opening (3) is formed in one side of the bath body; a slag discharge opening (5) is formed in the bottom of the bath body; the bottom of the bath body is made of reinforced macro-molecule polypropylene. According to the manganese electrolysis bath disclosed by the utility model: the special anode slag overflow opening is formed in the bottom of the bath body, so that the cleaning of the anode slag is facilitated, the condition of the electrolysis bath is greatly improved, management on the bath surface of the electrolysis bath is facilitated, and the labor intensity of workers is reduced; in addition, the corrosion resistance is achieved, the treatment such correction prevention is not required to be performed during the using process, and the correction prevention cost is reduced.
Description
Technical field
The utility model relates to Metal smelting field, relates in particular to a kind of novel manganese electrolytic cell.
Background technology
The main following pattern of electrolyzer of existing electrolytic metal Mn: wooden electrolyzer adds PVC soft plastic plate, and reinforced concrete electrolyzer adds Low Density Polyethylene rotational moulding liner.These electrolyzers easily cause cell body to puncture, and increase considerably cell body leaky, increase power consumption, and the maintenance of electrolyzer is simultaneously frequent, and work-ing life is short, increases the consumption of various materials.Electrolyzer electric leakage causes workman's safety coefficient to reduce.Electrolyzer damages leakage and causes the pollution to environment.Above factor cause the material consumption of electrolytic manganese industry and energy consumption high, cost rise, make business economic profit can not get maximize.Be not provided with slag-drip opening and have following shortcoming: 1. increase the amount of labour used; 2. workman's labour intensity is large; 3, cause the impact on environment in scarfing cinder process; 4, the groove time is long clearly, and impact is back to the groove condition of groove.
Utility model content
The purpose of this utility model is exactly the problem existing for prior art, and a kind of novel manganese electrolytic cell is provided, and it can control the factors such as electric leakage and maintenance cost, the energy-saving consumption-reducing object reaching.
Above-mentioned purpose realizes by following proposal:
A kind of manganese electrolytic cell, is characterized in that, described electrolyzer comprises cell body (8), diaphragm frame (1), false underframe and the vacation end (7), anolyte compartment (6); Be provided with anolyte overflow port (3) in cell body one side, be provided with slag-drip opening (5) in cell body bottom; The bottom of described cell body is used RPP polymer polypropylene material.
According to above-mentioned electrolyzer, it is characterized in that, described slag-drip opening (5) is the circular hole of diameter 100mm.
According to above-mentioned electrolyzer, it is characterized in that, described cell body bottom surrounding is to intermediate, inclined, and angle of inclination is less than 5 ‰ degree.
According to above-mentioned electrolyzer, it is characterized in that, the height of described anolyte compartment (6) is 30cm, (7) width of the described false end is 50mm.
The beneficial effects of the utility model:
The utility model has special anode slag overflow port in bottom land bottom, is convenient to clear up anode slag, greatly improves electrolytic bath condition, is convenient to electrolyzer surface management, has reduced workman's labour intensity.And, the utlity model has erosion resistance, in use procedure, without carrying out the anticorrosion processing of Denging, reduce anticorrosion cost.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Referring to Fig. 1, manganese electrolytic cell cell body of the present utility model (8), diaphragm frame 1, false underframe and the false end 7, anolyte compartment 6; Be provided with anolyte overflow port 3 in cell body one side, be provided with slag-drip opening 5 in cell body bottom; The bottom of described cell body is used RPP polymer polypropylene material.The false end 7 and false underframe, the installation of the false end 7 and anolyte compartment 6 is all that integral solder forms, whole like this electrolyzer good seal can be stopped the leakage accident of electrolyzer, greatly improves safety coefficient.The circular hole of slag-drip opening 5 preferred diameter 100mm, it is convenient to clear up anode slag, greatly improves electrolytic bath condition, is convenient to electrolyzer surface management, has reduced workman's labour intensity.
Adopt novel RPP polymer polypropylene material welding electrolyzer, have the following advantages: 1, fire resistance: there is stronger flame retardant resistance, minimum at similar middle cigarette poison.2, the type of resistance to marquis: material cross-linking density is high, good stability, long service life.3, erosion resistance: erosion resistance is strong, substantially indeformable after immersion, do not chap.4, nontoxicity: material does not have any toxic substance.At high temperature be difficult for decomposing, also can not produce obnoxious flavour.5, resiliency: its impact resistance of heat-insulation material is strong, not fragile.6, insulation level: have higher insulation level, prevent that cell body from puncturing, reduce the generation of cell body leaky, electrolyzer internal resistance is little, and power consumption is low, can save power consumption 10%, realizes the maximization of enterprise profit thereby reduce production costs.
Cell body bottom surrounding is thought intermediate, inclined, and angle of inclination is less than 5 ‰ degree, and not affecting, integral channel is external, is conducive to anode slag and collects.The height of anolyte compartment 6 is 30cm, is convenient to the control of electrolytic bath condition, is conducive to precipitation and the recovery of anode slag.Width of the described false ends 7 is 50mm, is convenient to so the fixing and sealing of diaphragm frame, avoids anode and cathode to alter mutually phenomenon, is conducive to the stable of groove condition.
Claims (4)
1. a manganese electrolytic cell, is characterized in that, described electrolyzer comprises cell body (8), diaphragm frame (1), false underframe and the vacation end (7), anolyte compartment (6); Be provided with anolyte overflow port (3) in cell body one side, be provided with slag-drip opening (5) in cell body bottom; The bottom of described cell body is used RPP polymer polypropylene material.
2. electrolyzer according to claim 1, is characterized in that, described slag-drip opening (5) is the circular hole of diameter 100mm.
3. electrolyzer according to claim 1, is characterized in that, described cell body bottom surrounding is to intermediate, inclined, and angle of inclination is less than 5 ‰ degree.
4. electrolyzer according to claim 1, is characterized in that, the height of described anolyte compartment (6) is 30cm, and (7) width of the described false end is 50mm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320708757.7U CN203593795U (en) | 2013-11-12 | 2013-11-12 | Manganese electrolysis bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320708757.7U CN203593795U (en) | 2013-11-12 | 2013-11-12 | Manganese electrolysis bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203593795U true CN203593795U (en) | 2014-05-14 |
Family
ID=50674693
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320708757.7U Expired - Lifetime CN203593795U (en) | 2013-11-12 | 2013-11-12 | Manganese electrolysis bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203593795U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104388979A (en) * | 2014-11-28 | 2015-03-04 | 刘益宏 | Electrolytic manganese production process |
| CN105603455A (en) * | 2016-02-26 | 2016-05-25 | 武汉大学 | Electrolytic tank for electrolytic manganese production |
| CN105671597A (en) * | 2016-02-04 | 2016-06-15 | 周勇 | Turbulent electrolytic cell and turbulent electrolytic production system consisting of turbulent electrolytic cell |
-
2013
- 2013-11-12 CN CN201320708757.7U patent/CN203593795U/en not_active Expired - Lifetime
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104388979A (en) * | 2014-11-28 | 2015-03-04 | 刘益宏 | Electrolytic manganese production process |
| CN105671597A (en) * | 2016-02-04 | 2016-06-15 | 周勇 | Turbulent electrolytic cell and turbulent electrolytic production system consisting of turbulent electrolytic cell |
| CN105671597B (en) * | 2016-02-04 | 2018-06-22 | 周勇 | A kind of turbulent flow electrolytic cell, the turbulent flow electrolysis production system being made of turbulent flow electrolytic cell |
| CN105603455A (en) * | 2016-02-26 | 2016-05-25 | 武汉大学 | Electrolytic tank for electrolytic manganese production |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C53 | Correction of patent of invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Jia Tianjiang Inventor after: Zhang Zhihua Inventor after: Tian Zhen Inventor after: Zou Xing Inventor before: Jia Tianjiang |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: INVENTOR; FROM: JIA TIANJIANG TO: JIA TIANJIANG ZHANG ZHIHUA TIAN ZHEN ZOU XING |
|
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Manganese electrolytic cell equipment Effective date of registration: 20150721 Granted publication date: 20140514 Pledgee: Bank of Jinzhou, Limited by Share Ltd Montenegro subbranch Pledgor: NINGXIA TIANYUAN MANGANESE Ltd. Registration number: 2015110000006 |
|
| PLDC | Enforcement, change and cancellation of contracts on pledge of patent right or utility model | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140514 |
|
| CX01 | Expiry of patent term |