CN108910958A - A method of manganese sulfate is produced using aniline reduction electrolytic manganese anode mud - Google Patents

A method of manganese sulfate is produced using aniline reduction electrolytic manganese anode mud Download PDF

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Publication number
CN108910958A
CN108910958A CN201810783452.XA CN201810783452A CN108910958A CN 108910958 A CN108910958 A CN 108910958A CN 201810783452 A CN201810783452 A CN 201810783452A CN 108910958 A CN108910958 A CN 108910958A
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manganese
slurry
manganese sulfate
added
aniline
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CN201810783452.XA
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Inventor
黎树春
廖新仁
马俊才
赵飞
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CHONGQING SHANGJIA ELECTRONIC CO LTD
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CHONGQING SHANGJIA ELECTRONIC CO LTD
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G45/00Compounds of manganese
    • C01G45/10Sulfates
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C50/00Quinones
    • C07C50/02Quinones with monocyclic quinoid structure
    • C07C50/04Benzoquinones, i.e. C6H4O2
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B13/00Obtaining lead
    • C22B13/04Obtaining lead by wet processes
    • C22B13/045Recovery from waste materials
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B25/00Obtaining tin
    • C22B25/04Obtaining tin by wet processes
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B25/00Obtaining tin
    • C22B25/06Obtaining tin from scrap, especially tin scrap
    • 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
    • C22B7/00Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
    • C22B7/006Wet processes
    • C22B7/007Wet processes by acid leaching
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Manufacturing & Machinery (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Inorganic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The invention discloses a kind of methods using aniline reduction electrolytic manganese anode mud production manganese sulfate, include the following steps:S1 adds the broken slurrying of water mill in Manganese anode slime;S2 imports manganese slurry in the reaction kettle with cooling device;Aniline is added in manganese slurry in S3;Manganese slurry is heated to 90~130 degrees Celsius, the benzoquinone after collecting vaporization by S4;S5 obtains slicker solder slag and manganese sulfate solution by manganese slurry by filter press separating and filtering;Ammonium sulfide is added in manganese sulfate solution obtained after separation by S6, is removed the heavy metals such as the lead in manganese sulfate solution, is obtained the higher manganese sulfate solution of purity;S7 by the heated concentration of purified manganese sulfate solution, Crystallization Separation, dries to obtain finished solid manganese sulfate.Elements and a small amount of manganese such as lead, tin, the antimony in the former earth of positive pole are only remained after benzoquinone of the present invention, manganese are recovered, in slag, because the quantity of slag significantly tails off, therefore in slag slicker solder antimony content significantly increase and by enriching and recovering.

Description

A method of manganese sulfate is produced using aniline reduction electrolytic manganese anode mud
Technical field
The present invention relates to a kind of methods using aniline reduction electrolytic manganese anode mud production manganese sulfate, belong to the life of manganese sulfate Produce preparation technical field.
Background technique
When being electrolysed manganese sulfate, there is a manganese metal and the earth of positive pole, manganese metal is used as the deep processing of manganese, and the earth of positive pole its mainly Ingredient is MnO2, and containing valuable metals such as lead, tin, antimony, it is generally industrially regarded into pyrolusite raw material, using iron powder reducing Method, ferrous sulfate reduction leaching process, two mines roasting water seaoning or two mine One-step production manganese sulfates.But no matter which kind of side used Method, because solid reductant is added, the leaching quantity of slag after soaking manganese is larger, causes the tenors such as lead, tin, the antimony in slag lower, returns It is big to receive difficulty, cost recovery is high, and without economic significance, therefore current domestic production producer is substantially by the way of landfill Reason, leads to the wasting of resources and environmental pollution.
Summary of the invention
The object of the present invention is to provide a kind of methods using aniline reduction electrolytic manganese anode mud production manganese sulfate, adopt Manganese, benzoquinone have not only been recycled with this method, but also has recycled the valuable elements such as the lead in the earth of positive pole to the greatest extent, together When perfectly solve the Manganese anode slime bring wasting of resources of electrolytic manganese manufacturer and problem of environmental pollution.
In order to solve the above technical problems, the present invention adopts the following technical scheme that:
A method of manganese sulfate being produced using aniline reduction electrolytic manganese anode mud, is included the following steps:
S1 adds water slurrying in Manganese anode slime;Below levigate extremely -120 mesh of Manganese anode slime;
S2 imports manganese slurry in the reaction kettle with cooling device, measures the volume of manganese slurry in reaction kettle, detection manganese slurry Solid-to-liquid ratio (guaranteeing the initial acid concentrations being added in 400~500g/l) and manganese dioxide content, are added according to manganese dioxide content Sulfuric acid solution (dosage of sulfuric acid be theoretical amount 1~2 times);
S3, by reactor temperature control at 30 degrees Celsius hereinafter, manganese slurry in aniline is added, after having added aniline, It is reacted 2~10 hours under normal temperature state;
MnO2+C6H7N+H2SO4→MnSO4+C6H4O2+H2O
Manganese slurry is heated to 90~130 degrees Celsius by S4, and the benzoquinone after collecting vaporization, temperature is too low, and benzoquinone is not It can vaporize completely, the excessively high benzoquinone of temperature will appear coking phenomenon, both will affect the rate of recovery of benzoquinone, using this The rate of recovery of method benzoquinone is up to 97% or more;
S5, by manganese slurry be cooled to 55 degrees Celsius or less (temperature is excessively high, in ammonium hydroxide with when ammonium hydroxide volatilization loss it is larger), Ammonium hydroxide is added in manganese slurry, the pH value that manganese is starched is adjusted to 5~7, and (under this pH condition, the impurity other than manganese is deposited in solid form ), by manganese slurry by filter press separating and filtering, obtain slicker solder slag (lead, tin the rate of recovery can achieve 99% or more) and sulfuric acid Manganese solution;
Appropriate ammonium sulfide will be added in S6 in manganese sulfate solution, further purification removes the heavy metals such as lead;
MeSO4+(NH4)2S→MeS+(NH4)2SO4, Me indicates the heavy metals such as lead in this chemical formula.
Purified manganese sulfate solution is obtained finished solid sulfuric acid by heating evaporation concentration, Crystallization Separation, drying by S7 Manganese.
In a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate above-mentioned, the step S6 further includes Following methods:The manganese sulfate solution is collected, ammonium sulfide solution is added in manganese sulfate solution, removes the lead in manganese sulfate solution Equal heavy metals.
In a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate above-mentioned, the step S1 further includes Following methods:Manganese anode slime particle is milled to -120 mesh hereinafter, then adding water slurrying.
In a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate above-mentioned, the Manganese anode slime is electricity The Manganese anode slime generated when solving manganese.
In a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate above-mentioned, aniline is no more than anti- Answer in kettle controlled at controlling value, aniline is added in manganese slurry.
Compared with prior art, lead, the tin, antimony in the former earth of positive pole are only remained after benzoquinone of the present invention, manganese are recovered, in slag Equal elements and a small amount of manganese, because the quantity of slag significantly tails off, therefore in slag slicker solder antimony content significantly increase and by enriching and recovering.The technique one It lifts three to obtain, has not only recycled manganese, benzoquinones, but also recycled the valuable elements such as the lead in the earth of positive pole to the greatest extent, while complete Beauty solves the Manganese anode slime bring wasting of resources of electrolytic manganese manufacturer and problem of environmental pollution.
The present invention is further illustrated With reference to embodiment.
Specific embodiment
The embodiment of the present invention 1:A method of manganese sulfate being produced using aniline reduction electrolytic manganese anode mud, including following Step:
S1 adds water slurrying in Manganese anode slime, and Manganese anode slime is levigate to -120 mesh;
S2 imports manganese slurry in the reaction kettle with cooling device, measures the volume of manganese slurry in reaction kettle, detection manganese slurry Sulfuric acid solution is added according to manganese dioxide content in solid-to-liquid ratio and manganese dioxide content;Guarantee the initial acid concentrations being added in 400g/ L, the dosage of sulfuric acid are 1 times of theoretical amount;
Reactor temperature is controlled at 30 degrees Celsius, aniline is added in manganese slurry, after having added aniline, in room temperature by S3 Reacted 2 hours under state, by aniline be no more than in reaction kettle controlled at controlling value, aniline is added in manganese slurry;
Manganese slurry is heated to 90 degrees Celsius, the benzoquinone after collecting vaporization by S4;
Manganese slurry is cooled to 55 degrees Celsius, ammonium hydroxide is added in manganese slurry, the pH value that manganese is starched is adjusted to 5, manganese slurry is passed through by S5 Filter press separating and filtering obtains slicker solder slag and manganese sulfate solution;
Ammonium sulfide is added in manganese sulfate solution obtained after separation by S6, removes the heavy metals such as the lead in manganese sulfate solution, The higher manganese sulfate solution of purity is obtained, the manganese sulfate solution is collected, ammonium sulfide solution is added in manganese sulfate solution, go sulphur removal Heavy metal in sour manganese solution;
S7 by the heated concentration of purified manganese sulfate solution, Crystallization Separation, dries to obtain finished solid manganese sulfate.
Embodiment 2:A method of manganese sulfate being produced using aniline reduction electrolytic manganese anode mud, is included the following steps:
Then plus water slurrying S1, the Manganese anode slime particle generated when by electrolytic manganese are milled to -150 mesh,;
S2 imports manganese slurry in the reaction kettle with cooling device, measures the volume of manganese slurry in reaction kettle, detection manganese slurry Sulfuric acid solution is added according to manganese dioxide content in solid-to-liquid ratio and manganese dioxide content;Guarantee the initial acid concentrations being added in 500g/ L, the dosage of sulfuric acid are 2 times of theoretical amount;
Reactor temperature is controlled at 20 degrees Celsius, aniline is added in manganese slurry, after having added aniline, in room temperature by S3 Reacted 10 hours under state, by aniline be no more than in reaction kettle controlled at controlling value, aniline is added in manganese slurry;
Manganese slurry is heated to 130 degrees Celsius, the benzoquinone after collecting vaporization by S4;
Manganese slurry is cooled to 45 degrees Celsius, ammonium hydroxide is added in manganese slurry, the pH value that manganese is starched is adjusted to 7, manganese slurry is passed through by S5 Filter press separating and filtering obtains slicker solder slag and manganese sulfate solution;
Ammonium sulfide is added in manganese sulfate solution obtained after separation by S6, removes the heavy metals such as the lead in manganese sulfate solution, The higher manganese sulfate solution of purity is obtained, the manganese sulfate solution is collected, ammonium sulfide solution is added in manganese sulfate solution, go sulphur removal Heavy metal in sour manganese solution;
S7 by the heated concentration of purified manganese sulfate solution, Crystallization Separation, dries to obtain finished solid manganese sulfate.
Embodiment 3:A method of manganese sulfate being produced using aniline reduction electrolytic manganese anode mud, is included the following steps:
Then plus water slurrying S1, the Manganese anode slime particle generated when by electrolytic manganese are milled to -160 mesh,;
S2 imports manganese slurry in the reaction kettle with cooling device, measures the volume of manganese slurry in reaction kettle, detection manganese slurry Sulfuric acid solution is added according to manganese dioxide content in solid-to-liquid ratio and manganese dioxide content;Guarantee the initial acid concentrations being added in 430g/ L, the dosage of sulfuric acid are 1.4 times of theoretical amount;
Reactor temperature is controlled at 25 degrees Celsius, aniline is added in manganese slurry, after having added aniline, in room temperature by S3 Reacted 7 hours under state, by aniline be no more than in reaction kettle controlled at controlling value, aniline is added in manganese slurry;
Manganese slurry is heated to 110 degrees Celsius, the benzoquinone after collecting vaporization by S4;
Manganese slurry is cooled to 35 degrees Celsius, ammonium hydroxide is added in manganese slurry, the pH value that manganese is starched is adjusted to 6, manganese slurry is passed through by S5 Filter press separating and filtering obtains slicker solder slag and manganese sulfate solution;
Ammonium sulfide is added in manganese sulfate solution obtained after separation by S6, removes the heavy metals such as the lead in manganese sulfate solution, The higher manganese sulfate solution of purity is obtained, the manganese sulfate solution is collected, ammonium sulfide solution is added in manganese sulfate solution, go sulphur removal Heavy metal in sour manganese solution;
S7 by the heated concentration of purified manganese sulfate solution, Crystallization Separation, dries to obtain finished solid manganese sulfate.

Claims (6)

1. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate, which is characterized in that include the following steps:
S1 adds water slurrying in Manganese anode slime;
S2 imports manganese slurry in the reaction kettle with cooling device, measures the volume of manganese slurry in reaction kettle, the solid-liquid of detection manganese slurry Than with manganese dioxide content, according to manganese dioxide content be added sulfuric acid solution;
S3 controls reactor temperature at 30 degrees Celsius hereinafter, aniline is added in manganese slurry, after having added aniline, in room temperature It is reacted 2~10 hours under state;
Manganese slurry is heated to 90~130 degrees Celsius, the benzoquinone after collecting vaporization by S4;
S5, by manganese slurry be cooled to 55 degrees Celsius hereinafter, manganese slurry in ammonium hydroxide is added, by manganese starch pH value be adjusted to 5~7, manganese is starched By filter press separating and filtering, slicker solder slag and manganese sulfate solution are obtained;
Ammonium sulfide is added in manganese sulfate solution obtained after separation by S6, is removed the heavy metals such as the lead in manganese sulfate solution, is obtained pure Spend higher manganese sulfate solution;
S7 by the heated concentration of purified manganese sulfate solution, Crystallization Separation, dries to obtain finished solid manganese sulfate.
2. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate according to claim 1, feature It is, the step S6 further includes following methods:The manganese sulfate solution is collected, it is molten that ammonium sulfide is added in manganese sulfate solution Liquid removes the heavy metal in manganese sulfate solution.
3. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate according to claim 1, feature It is, the step S1 further includes following methods:Manganese anode slime particle is milled to -120 mesh hereinafter, then adding water slurrying.
4. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate according to claim 1, feature It is, the Manganese anode slime that the Manganese anode slime generates when being electrolytic manganese.
5. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate according to claim 1, feature It is, further includes following methods in the step S3:By aniline be no more than reaction kettle in controlled at controlling value, by benzene Amine is added in manganese slurry.
6. a kind of method using aniline reduction electrolytic manganese anode mud production manganese sulfate according to claim 1, feature It is, further includes following methods in the step S2:The solid-to-liquid ratio and manganese dioxide content for detecting manganese slurry, contain according to manganese dioxide Sulfuric acid solution is added in amount;Guarantee the initial acid concentrations being added in 400~500g/l, the dosage of sulfuric acid is 1~2 times of theoretical amount.
CN201810783452.XA 2018-07-17 2018-07-17 A method of manganese sulfate is produced using aniline reduction electrolytic manganese anode mud Pending CN108910958A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113387391A (en) * 2021-07-30 2021-09-14 广西埃索凯新材料科技有限公司 Manganese sulfate production system based on manganese oxide ore
CN115011799A (en) * 2022-07-13 2022-09-06 重庆上甲电子股份有限公司 Method for producing soft magnetic trimanganese tetroxide by using electrolytic manganese anode slime
CN115058600A (en) * 2022-07-21 2022-09-16 贵州大学 Method for preparing manganese sulfate solution and recycling lead from anode slag
CN115386744A (en) * 2022-08-18 2022-11-25 铜仁学院 Method for high-value utilization of manganese anode slime

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1121049A (en) * 1994-10-18 1996-04-24 冶金工业部长沙矿冶研究院 Method for producing high-purity manganese carbonate by using pyrolusite
CN1126246A (en) * 1994-10-28 1996-07-10 北京矿冶研究总院 Arylamine reduction leaching method for marine manganese nodule
CN1657423A (en) * 2005-02-01 2005-08-24 桂林市孟泰矿产技术开发有限责任公司 Method of recovering manganese sulfate from low-grade manganese carbonate and manganese oxide
CN1884099A (en) * 2006-07-07 2006-12-27 广西大学 Method for preparing manganese sulfate by reduction leaching of manganese ore using discard molasses and sulfuric acid
CN101412543A (en) * 2008-11-18 2009-04-22 湖北开元化工科技股份有限公司 Preparation of high purity manganese sulfate
CN102780014A (en) * 2012-08-09 2012-11-14 遵义师范学院 Method for regenerating manganese sulfate from waste alkaline zinc-manganese battery
CN103789551A (en) * 2014-02-18 2014-05-14 广西大学 Method for preparing manganese sulfate electrolyte and recycling lead by using electrolytic manganese anode mud

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1121049A (en) * 1994-10-18 1996-04-24 冶金工业部长沙矿冶研究院 Method for producing high-purity manganese carbonate by using pyrolusite
CN1126246A (en) * 1994-10-28 1996-07-10 北京矿冶研究总院 Arylamine reduction leaching method for marine manganese nodule
CN1657423A (en) * 2005-02-01 2005-08-24 桂林市孟泰矿产技术开发有限责任公司 Method of recovering manganese sulfate from low-grade manganese carbonate and manganese oxide
CN1884099A (en) * 2006-07-07 2006-12-27 广西大学 Method for preparing manganese sulfate by reduction leaching of manganese ore using discard molasses and sulfuric acid
CN101412543A (en) * 2008-11-18 2009-04-22 湖北开元化工科技股份有限公司 Preparation of high purity manganese sulfate
CN102780014A (en) * 2012-08-09 2012-11-14 遵义师范学院 Method for regenerating manganese sulfate from waste alkaline zinc-manganese battery
CN103789551A (en) * 2014-02-18 2014-05-14 广西大学 Method for preparing manganese sulfate electrolyte and recycling lead by using electrolytic manganese anode mud

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113387391A (en) * 2021-07-30 2021-09-14 广西埃索凯新材料科技有限公司 Manganese sulfate production system based on manganese oxide ore
CN115011799A (en) * 2022-07-13 2022-09-06 重庆上甲电子股份有限公司 Method for producing soft magnetic trimanganese tetroxide by using electrolytic manganese anode slime
CN115058600A (en) * 2022-07-21 2022-09-16 贵州大学 Method for preparing manganese sulfate solution and recycling lead from anode slag
CN115386744A (en) * 2022-08-18 2022-11-25 铜仁学院 Method for high-value utilization of manganese anode slime
CN115386744B (en) * 2022-08-18 2024-02-02 铜仁学院 Method for high-value utilization of manganese anode slime

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Inventor after: Li Shuchun

Inventor after: Fu Jing

Inventor after: Liao Xinren

Inventor after: Ma Juncai

Inventor after: Zhao Fei

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Application publication date: 20181130