CN107513625A - A kind of impurity-removing method of electrolytic manganese dioxide - Google Patents

A kind of impurity-removing method of electrolytic manganese dioxide Download PDF

Info

Publication number
CN107513625A
CN107513625A CN201710905149.8A CN201710905149A CN107513625A CN 107513625 A CN107513625 A CN 107513625A CN 201710905149 A CN201710905149 A CN 201710905149A CN 107513625 A CN107513625 A CN 107513625A
Authority
CN
China
Prior art keywords
impurity
container
removing method
manganese dioxide
interior axle
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.)
Pending
Application number
CN201710905149.8A
Other languages
Chinese (zh)
Inventor
黎超英
吴沛荣
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.)
Liuzhou Kaitong New Material Technology Co Ltd
Original Assignee
Liuzhou Kaitong New Material Technology 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 Liuzhou Kaitong New Material Technology Co Ltd filed Critical Liuzhou Kaitong New Material Technology Co Ltd
Priority to CN201710905149.8A priority Critical patent/CN107513625A/en
Publication of CN107513625A publication Critical patent/CN107513625A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B47/00Obtaining manganese
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/22Treatment or purification of solutions, e.g. obtained by leaching by physical processes, e.g. by filtration, by magnetic means, or by thermal decomposition
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B3/00Extraction of metal compounds from ores or concentrates by wet processes
    • C22B3/20Treatment or purification of solutions, e.g. obtained by leaching
    • C22B3/44Treatment or purification of solutions, e.g. obtained by leaching by chemical processes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/21Manganese oxides

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Abstract

The present invention relates to a kind of impurity-removing method of electrolytic manganese dioxide, and it, which is used, inputs manganese sulfate leachate to container, adds barium sulphide, starts the stirring rod being arranged on outer shaft and is stirred, precipitates solution;Outer shaft is lifted up, make to be arranged on hollow interior axle in outer shaft close to the container bottom one section exposes;One section interior axle of the solution through exposing in container filters out precipitation;Filtrate after filtering is flowed out from interior axle inner chamber, and the filtrate of outflow enters the purification being arranged on the downside of container and purified, and after the completion of reaction, filtered device filters precipitation, is purified liquid.The present invention is filtered using the inside and outside axle for driving stirring rod to rotate to solution, and on the one hand the leachate that add barium sulphide can be stirred, and makes its reaction generation precipitation;On the other hand interior axle is entered filtering to leachate by lifting outer shaft, so as to which precipitation is retained in container, is achieved that stirring, filtering without other auxiliary equipments, substantially increases production efficiency.

Description

A kind of impurity-removing method of electrolytic manganese dioxide
Technical field
The present invention relates to a kind of impurity-removing method of electrolytic manganese dioxide.
Background technology
Mainly include manganese oxide ore and manganese carbonate ore with industrial application value in natural manganese ore, according to the taste of manganese ore It is internal and international at present that deep processing processing typically is carried out to it using two kinds of processes with the difference of impurity content:When pair In objectionable impurities(Such as phosphorus, sulphur)Low high-grade ore can be directly using pyrometallurgical smelting process production Mn series alloy product or as battery Manganese powder;Second, for most of manganese carbonate and partial oxidation manganese ore, the general serial salt using hydrometallurgical technology production manganese Product.However, with the exploitation year by year to manganese resource, GOOD TASTE, the ANOMALY IN FINE QUALITY MANGANESE DEPOSITS increasingly depleted of low impurity, therefore, for The research and development and utilization for the complicated manganese ore that manganese content is low, impurity content is high, which turn into, improves domestic manganese ore deep processing enterprise in the world The key of the market competitiveness, also largely determine that can manganese ore processing industry sustainable development.Electricity is prepared existing During solving manganese dioxide, impurity and purification need to be carried out to middle the product sulfur acid manganese solution, and current manganese sulfate electrolyte Clarification time is grown, and influences production efficiency.
The content of the invention
For above-mentioned technical problem, the present invention provides a kind of removal of impurities side for the electrolytic manganese dioxide for improving production efficiency Method.
Technical scheme is used by the present invention solves above-mentioned technical problem:A kind of impurity-removing method of electrolytic manganese dioxide, It uses the following steps:
(1)Manganese sulfate leachate is inputted to container, adds barium sulphide, starts the stirring rod being arranged on outer shaft and is stirred Mix, precipitate solution;
(2)Outer shaft is lifted up, make to be arranged on hollow interior axle in outer shaft close to the container bottom one section exposes;
(3)One section interior axle of the solution through exposing in container filters out precipitation;
(4)Filtrate after filtering is flowed out from interior axle inner chamber;
(5)The filtrate of outflow enters the clarifier-tank being arranged on the downside of container;
(6)Sodium Dimethyldithiocarbamate and filtrate reaction generation precipitation are added in clarifier-tank;
(7)After the completion of reaction, the filter in purified bottom of pond portion filters precipitation, is purified liquid.
Preferably, 8g barium sulphides are added in every liter of manganese sulfate leachate.
Preferably, mixing time 45min.
Preferably, the interior axle bottom exposed is provided with the opening that connect with its inner chamber, be open on covered with filter screen.
Preferably, it is provided with stirring slurry in the clarifier-tank.
Preferably, the amount of Sodium Dimethyldithiocarbamate is every liter of solution 1g.
Preferably, the filter includes the seal cover board for being arranged on clarifier-tank bottom and being flexibly connected, on cover plate It is provided with filter plate.
As can be known from the above technical solutions, the present invention is filtered using the inside and outside axle for driving stirring rod to rotate to solution, and one Aspect can be stirred to the leachate for adding barium sulphide, make its reaction generation precipitation;On the other hand made by lifting outer shaft Interior axle enters filtering to leachate, and so as to which precipitation is retained in container, stirring, mistake are achieved that without other auxiliary equipments Filter, substantially increases production efficiency.
Embodiment
The present invention is described in detail below, illustrative examples of the invention and explanation are used for explaining the present invention herein, but It is not as a limitation of the invention.
A kind of impurity-removing method of electrolytic manganese dioxide, it uses the following steps:
First, manganese sulfate leachate is inputted to container, adds barium sulphide, 8g vulcanizations are added in about every liter manganese sulfate leachate Barium, ensure the generation of precipitation.Then, start the stirring rod being arranged on outer shaft to be stirred, outer shaft is driven by motor to be rotated, real Now automation stirring, is stirred while precipitating solution;
After stir about 45min, outer shaft is lifted up, makes to be arranged on the hollow interior axle in outer shaft close to one section of the container bottom Expose;In implementation process, the interior axle bottom exposed is provided with opening connect with its inner chamber, be open on covered with filter screen, container Interior solution filters precipitation through filter screen, and the filtrate after filtering is flowed out from interior axle inner chamber.
In implementation process, interior axle passes through container bottom, and can be arranged on bottom by bearing, and outer shaft is then not passed through container Bottom, inside and outside axle can be connected by flat key etc., so as to rotate simultaneously;When outer shaft drives stirring rod rotation, outer shaft blocks interior The opening of axle, prevent solution from being flowed out from opening.After outer shaft stops the rotation, outer shaft is lifted up, exposes opening;Now solution can be from The filter screen of opening flows into the inner chamber of interior axle, realizes filtering.In order to prevent precipitation from blocking filter screen, in filter process, interior axle can be made Rotation, precipitation is thrown away to interior axle outside using centrifugal force, avoid precipitation from being gathered near filter screen.
Enter the clarifier-tank being arranged on the downside of container from the filtrate of interior axle outflow, Sodium Dimethyldithiocarbamate is added in clarifier-tank to filtrate Purified.And the addition of Sodium Dimethyldithiocarbamate is every liter of solution 1g, and the stirring slurry that can be rotated with interior axle is provided with clarifier-tank, made The solution obtained in clarifier-tank fully precipitates, and realizes the purpose of purification.In implementation process, Sodium Dimethyldithiocarbamate heavy metal ion such as nickel There is good impurity-eliminating effect with cobalt, the concentration of iron ion is possible to or can not reach standard in purification process, this process Hydrogen peroxide can be also suitably added and remove standard to reach iron ion.
In implementation process, the filter includes the closure for being arranged on the clarifier-tank bottom and being flexibly connected Plate, filter plate is provided with cover plate;After the completion of the solution reaction in clarifier-tank, seal cover board can be opened, makes solution through filter plate mistake Filter filters off precipitation, is purified liquid, realizes that secondary filter cleans, greatly improves clean-up effect.From the above it can be seen that the present invention can be to electricity The manganese sulfate solution solved in dioxy manganese metal preparation process carries out continuous impurity and purification, can not only improve production efficiency, Er Qiecao Make convenient and simple, cost is low.
Above-mentioned embodiment is used for illustrative purposes only, and is not limitation of the present invention, relevant technical field Those of ordinary skill, can be so that various changes can be made and modification without departing from the spirit and scope of the present invention, therefore institute There is equivalent technical scheme also to belong to scope of the invention.

Claims (7)

1. a kind of impurity-removing method of electrolytic manganese dioxide, it uses the following steps:
(1)Manganese sulfate leachate is inputted to container, adds barium sulphide, starts the stirring rod being arranged on outer shaft and is stirred Mix, precipitate solution;
(2)Outer shaft is lifted up, make to be arranged on hollow interior axle in outer shaft close to the container bottom one section exposes;
(3)One section interior axle of the solution through exposing in container filters out precipitation;
(4)Filtrate after filtering is flowed out from interior axle inner chamber;
(5)The filtrate of outflow enters the clarifier-tank being arranged on the downside of container;
(6)Sodium Dimethyldithiocarbamate and filtrate reaction generation precipitation are added in clarifier-tank;
(7)After the completion of reaction, the filter in purified bottom of pond portion filters precipitation, is purified liquid.
2. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:Add in every liter of manganese sulfate leachate Enter 8g barium sulphides.
3. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:Mixing time 45min.
4. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:The interior axle bottom exposed be provided with Its inner chamber connection opening, opening on covered with filter screen.
5. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:Stirring is provided with the clarifier-tank Slurry.
6. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:The amount of Sodium Dimethyldithiocarbamate is every liter of solution 1g。
7. the impurity-removing method of electrolytic manganese dioxide according to claim 1, it is characterised in that:The filter includes setting Filter plate is provided with clarifier-tank bottom and the seal cover board of flexible connection, cover plate.
CN201710905149.8A 2017-09-30 2017-09-30 A kind of impurity-removing method of electrolytic manganese dioxide Pending CN107513625A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710905149.8A CN107513625A (en) 2017-09-30 2017-09-30 A kind of impurity-removing method of electrolytic manganese dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710905149.8A CN107513625A (en) 2017-09-30 2017-09-30 A kind of impurity-removing method of electrolytic manganese dioxide

Publications (1)

Publication Number Publication Date
CN107513625A true CN107513625A (en) 2017-12-26

Family

ID=60725764

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710905149.8A Pending CN107513625A (en) 2017-09-30 2017-09-30 A kind of impurity-removing method of electrolytic manganese dioxide

Country Status (1)

Country Link
CN (1) CN107513625A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101684562A (en) * 2008-09-28 2010-03-31 熊一言 Liquid making technique for manganese oxide ore
CN103194767A (en) * 2013-04-16 2013-07-10 中南大学 Method for preparing manganese sulfate electrolyte by using high-iron and high-phosphor manganese ores
CN103233119A (en) * 2013-04-25 2013-08-07 国土资源部长沙矿产资源监督检测中心 Process for producing manganese sulfate by treating two ores with acid
CN103496746A (en) * 2013-08-27 2014-01-08 中南大学 Method for preparing cell-grade high-purity manganese sulfate by low-grade manganese ore high-pressure crystallization
CN204583024U (en) * 2015-03-13 2015-08-26 广东弘和高新材料股份有限公司 A kind of paint mixing and filter

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101684562A (en) * 2008-09-28 2010-03-31 熊一言 Liquid making technique for manganese oxide ore
CN103194767A (en) * 2013-04-16 2013-07-10 中南大学 Method for preparing manganese sulfate electrolyte by using high-iron and high-phosphor manganese ores
CN103233119A (en) * 2013-04-25 2013-08-07 国土资源部长沙矿产资源监督检测中心 Process for producing manganese sulfate by treating two ores with acid
CN103496746A (en) * 2013-08-27 2014-01-08 中南大学 Method for preparing cell-grade high-purity manganese sulfate by low-grade manganese ore high-pressure crystallization
CN204583024U (en) * 2015-03-13 2015-08-26 广东弘和高新材料股份有限公司 A kind of paint mixing and filter

Similar Documents

Publication Publication Date Title
CN104911359B (en) A kind of process that cobalt and nickel are extracted from manganese waste slag
CN103014760B (en) Production method of electrolytic manganese metal
JP6070898B2 (en) Method and facility for recovering valuable components from waste dry batteries
CN105648214B (en) It is a kind of to control the method that current potential vulcanization separates valuable metal in solution
CN106350673B (en) A kind of method for controlling current potential selective precipitation separation cobalt
CN109136571B (en) Method for extracting valuable metals from lithium ion battery mixed manganese-rich waste leachate
CN106544511A (en) A kind of method of synthetical recovery manganese, lead, silver and selenium from Manganese anode slime
CN101871046A (en) Method for recycling heavy metal pollution wastes
CN103160688B (en) Zinc replacement prepares the method for germanium concentrate from germanic leach liquor
JP2015206077A (en) Method and apparatus for separating and recovering resource from waste dry cell and recovered substance
CN101497943B (en) Method for processing cobalt waste slag and recycling cobalt by sodium persulfate oxidation treatment
AU2018286479A1 (en) Method for the production of cobalt and associated oxides from various feed materials
CN106987721A (en) A kind of nothing of sludge containing heavy metal is given up Application way
CN106119560A (en) Zinc-cobalt separation method
CN103572313A (en) Production method for mercury-free alkaline-manganese type electrolytic manganese dioxide
CN110172583B (en) Method for efficiently treating arsenic-containing soot in reduction mode
CN108866337B (en) A method of processing metal sludge
CN102899491B (en) Method for floating and separating high-concentration iron ions from zinc sulfate leachate
CN107675201A (en) The preparation method of electrolytic manganese dioxide
JP6898586B2 (en) Sulfide leaching method
CN103395825B (en) A kind of method utilizing steel-smelting electric furnace flue dust to produce nano zine oxide
CN103221557B (en) Method for producing nickel-ontaining acidic solution
CN107513625A (en) A kind of impurity-removing method of electrolytic manganese dioxide
CN107419301A (en) A kind of preparation method of complex precipitant and a kind of purification method of copper electrolyte
CN107513615A (en) A kind of purification method of electrolytic manganese metal

Legal Events

Date Code Title Description
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20171226