CN102963937B - A kind of refining method of by-product Manganse Dioxide - Google Patents
A kind of refining method of by-product Manganse Dioxide Download PDFInfo
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- CN102963937B CN102963937B CN201210426958.8A CN201210426958A CN102963937B CN 102963937 B CN102963937 B CN 102963937B CN 201210426958 A CN201210426958 A CN 201210426958A CN 102963937 B CN102963937 B CN 102963937B
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- Prior art keywords
- mno
- manganse dioxide
- product
- refining method
- crude product
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Abstract
The invention discloses a kind of refining method of by-product Manganse Dioxide, concrete steps are as follows: first use 15-20% dilute sulphuric acid process crude product MnO
2, then add strong oxidizer ammonium persulphate oxide treatment aforesaid liquid, be heated to 45-50 DEG C, stir 20-30min, filter, wash, dry and obtain product purification Manganse Dioxide.The present invention effectively can utilize the MnO in production
2?waste material, by dissolve and its transformation of crystal is urged in the measure such as oxidation, increase that it is active, do utilization of waste material, turn waste into wealth, there is not secondary pollution, both added benefit, purified again environment.
Description
Technical field
The present invention relates to a kind of refining method of by-product Manganse Dioxide, belong to chemical technology field.
Background technology
The zinc subcarbonate demanganization stage can produce a large amount of Manganse Dioxide by-product, and Manganse Dioxide is a kind of well novel battery positive electrode material.In order to carry out utilization of waste material, my company develops Manganse Dioxide refining method.
Summary of the invention
The object of the invention is to the Manganse Dioxide by-product making full use of the generation of zinc subcarbonate demanganization, provide a kind of refining method of by-product Manganse Dioxide, for cell positive material.
The technical solution used in the present invention is as follows:
A refining method for by-product Manganse Dioxide, comprises the following steps:
(1) with 15-20% dilute sulphuric acid process crude product MnO
2, be wherein mingled in MnO
2mnCO
3or the solubilized such as MnO generates MnSO
4, crude product MnO simultaneously
2in a small amount of α, beta crystal to γ type transition, thus improve MnO
2activity and purity;
(2) oxide treatment aforesaid liquid, processed in the liquid containing Manganse Dioxide to step (1) and added 2-3% strong oxidizer ammonium persulphate, be heated to 45-50 DEG C, stirred 20-30min, the Mn in solution
2+change into MnO
2;
(3) solution step (2) processed filters, wash, dry and obtain product purification Manganse Dioxide.
Described dilute sulphuric acid and crude product MnO
2mol ratio be 1:3-4.
Aforesaid method reaction equation is as follows:
MnCO
3+H
2SO
4----→MnSO
4+H
2O+CO
2↑
MnO+H
2SO
4----→MnSO
4+H
2O
Mn
2O
3+H
2SO
4----→MnSO
4+MnO
2+H
2O
Mn
3O
4+H
2SO
4-----→MnO
2+MnSO
4+H
2O
MnSO
4+(NH
4)
2S
2O
8+H
2O-----→MnO
2+H
2SO
4+(NH
4)
2SH
4
Beneficial effect of the present invention:
The present invention effectively can utilize the MnO in production
2waste material, by dissolve and its transformation of crystal is urged in the measure such as oxidation, increase that it is active, do utilization of waste material, turn waste into wealth, there is not secondary pollution, both added benefit, purified again environment.
Embodiment
Embodiment
A refining method for by-product Manganse Dioxide, comprises the following steps:
(1) with 20% dilute sulphuric acid process crude product MnO
2, be wherein mingled in MnO
2mnCO
3or the solubilized such as MnO generates MnSO
4, crude product MnO simultaneously
2in a small amount of α, beta crystal to γ type transition, thus improve MnO
2activity and purity;
(2) oxide treatment aforesaid liquid, processed in the liquid containing Manganse Dioxide to step (1) and added 2% strong oxidizer ammonium persulphate, be heated to 50 DEG C, stirred 30min, the Mn in solution
2+change into MnO
2;
(3) solution step (2) processed filters, wash, dry and obtain product purification Manganse Dioxide.
Wherein, described dilute sulphuric acid and crude product MnO
2mol ratio be 1:4.
After testing, the Manganse Dioxide content after refining is 99.95%, meets national standard.
Claims (2)
1. a refining method for by-product Manganse Dioxide, is characterized in that comprising the following steps:
(1) with 15-20% dilute sulphuric acid process crude product MnO
2, be wherein mingled in MnO
2mnCO
3or MnO solubilized generates MnSO
4, crude product MnO simultaneously
2in a small amount of α, beta crystal to γ type transition, thus improve MnO
2activity and purity;
(2) oxide treatment aforesaid liquid, processed in the liquid containing Manganse Dioxide to step (1) and added 2-3% strong oxidizer ammonium persulphate, be heated to 45-50 DEG C, stirred 20-30min, the Mn in solution
2+change into MnO
2;
(3) solution step (2) processed filters, wash, dry and obtain product purification Manganse Dioxide.
2. the refining method of by-product Manganse Dioxide according to claim 1, is characterized in that, described dilute sulphuric acid and crude product MnO
2mol ratio be 1:3-4.
Priority Applications (1)
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CN201210426958.8A CN102963937B (en) | 2012-10-31 | 2012-10-31 | A kind of refining method of by-product Manganse Dioxide |
Applications Claiming Priority (1)
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---|---|---|---|
CN201210426958.8A CN102963937B (en) | 2012-10-31 | 2012-10-31 | A kind of refining method of by-product Manganse Dioxide |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102963937A CN102963937A (en) | 2013-03-13 |
CN102963937B true CN102963937B (en) | 2015-12-09 |
Family
ID=47794414
Family Applications (1)
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CN201210426958.8A Expired - Fee Related CN102963937B (en) | 2012-10-31 | 2012-10-31 | A kind of refining method of by-product Manganse Dioxide |
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Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105914380B (en) * | 2016-04-15 | 2018-07-27 | 广东工业大学 | A kind of metal-air battery oxygen electrode active material and its preparation method and application |
CN114275819B (en) * | 2021-12-16 | 2024-03-01 | 湖南化工研究院有限公司 | Efficient recovery method of active manganese dioxide |
CN114974910B (en) * | 2022-06-06 | 2024-03-22 | 安徽信息工程学院 | Electrode material and preparation method thereof |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102040248A (en) * | 2010-12-01 | 2011-05-04 | 湖南汇通科技有限责任公司 | Preparation method of active manganese dioxide |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07289906A (en) * | 1994-04-25 | 1995-11-07 | Daicel Chem Ind Ltd | Activation and oxidation of manganese dioxide |
-
2012
- 2012-10-31 CN CN201210426958.8A patent/CN102963937B/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102040248A (en) * | 2010-12-01 | 2011-05-04 | 湖南汇通科技有限责任公司 | Preparation method of active manganese dioxide |
Non-Patent Citations (3)
Title |
---|
天然轻质二氧化锰直接活化制备活性二氧化锰;袁明亮等;《矿产保护与利用》;20000831(第4期);第46-48页 * |
湿法制取活性氧化锌与化学二氧化锰新工艺研究(上);唐华雄等;《中国锰业》;19931231;第11卷(第6期);第26-30页 * |
湿法制取活性氧化锌与化学二氧化锰新工艺研究(下);唐华雄等;《中国锰业》;19941231;第12卷(第1期);第38-41页 * |
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