CN102963937B - A kind of refining method of by-product Manganse Dioxide - Google Patents

A kind of refining method of by-product Manganse Dioxide Download PDF

Info

Publication number
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
Authority
CN
China
Prior art keywords
mno
manganse dioxide
product
refining method
crude product
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
Application number
CN201210426958.8A
Other languages
Chinese (zh)
Other versions
CN102963937A (en
Inventor
张红英
周大明
王明祥
张后云
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TONGLING CITY XIANGYING ZINC INDUSTRY Co Ltd
Original Assignee
TONGLING CITY XIANGYING ZINC INDUSTRY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by TONGLING CITY XIANGYING ZINC INDUSTRY Co Ltd filed Critical TONGLING CITY XIANGYING ZINC INDUSTRY Co Ltd
Priority to CN201210426958.8A priority Critical patent/CN102963937B/en
Publication of CN102963937A publication Critical patent/CN102963937A/en
Application granted granted Critical
Publication of CN102963937B publication Critical patent/CN102963937B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Battery Electrode And Active Subsutance (AREA)

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

A kind of refining method of by-product Manganse Dioxide
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.
CN201210426958.8A 2012-10-31 2012-10-31 A kind of refining method of by-product Manganse Dioxide Expired - Fee Related CN102963937B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210426958.8A CN102963937B (en) 2012-10-31 2012-10-31 A kind of refining method of by-product Manganse Dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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)

Application Number Title Priority Date Filing Date
CN201210426958.8A Expired - Fee Related CN102963937B (en) 2012-10-31 2012-10-31 A kind of refining method of by-product Manganse Dioxide

Country Status (1)

Country Link
CN (1) CN102963937B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (1)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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 *

Also Published As

Publication number Publication date
CN102963937A (en) 2013-03-13

Similar Documents

Publication Publication Date Title
CN103401010B (en) Method for preparing electrolytes of all-vanadium flow battery
CN107857243A (en) The method that titanium white by product thing ferrous sulfate prepares LITHIUM BATTERY superfine iron phosphate
CN113307243B (en) Method for preparing iron phosphate by recycling mother liquor
CN114538404B (en) Method for preparing lithium iron phosphate from titanium white byproduct ferrous sulfate
CN104393364A (en) Method for preparing PbO from waste lead-acid battery by using direct wet method
CN113336212B (en) Method for preparing iron phosphate by recycling mother liquor
CN107032316A (en) A kind of preparation method of ferric phosphate
CN102963937B (en) A kind of refining method of by-product Manganse Dioxide
CN109928375B (en) Method for preparing iron phosphate by using monocalcium phosphate
CN103904343B (en) The preparation method of all-vanadium redox flow battery electrolytic solution
CN103022491A (en) Method for preparing lithium iron phosphate precursor for positive pole material of lithium-ion battery
CN107986252B (en) Method for preparing iron phosphate by using by-product ferrophosphorus
CN106450401B (en) A method of vanadic sulfate is prepared using discarded V electrolyte
CN103991912B (en) A kind of synthesis technique of PFAS
CN116259811B (en) Method for preparing vanadium electrolyte from sodium vanadate solution
CN104876274A (en) Preparation method of manganous-manganic oxide
CN107863531A (en) A kind of method that anode material for lithium-ion batteries is prepared using siderite
CN108394934A (en) A kind of V electrolyte high-purity oxyvanadium compound and preparation method thereof
CN107204456B (en) Preparation method of titanium-coated ternary cathode material
CN102969521A (en) Method for preparing positive electrode electrolyte of vanadium battery
CN112340719B (en) Method for preparing battery-grade iron phosphate by taking chloride as medium
CN108217739A (en) It is a kind of to prepare the method for manganese sulfate and its product obtained with troilite
CN107311853A (en) A kind of synthetic method of LITHIUM BATTERY oxalic acid ferromanganese
CN102534647A (en) Electrolyte solution for water electrolysis equipment and preparing method for electrolyte solution
CN106082347A (en) The preparation method of manganese dioxide

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
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: 20151209

Termination date: 20161031