CN108441888A - A kind of tin electrorefining electrolyte compound additive - Google Patents

A kind of tin electrorefining electrolyte compound additive Download PDF

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Publication number
CN108441888A
CN108441888A CN201810460439.0A CN201810460439A CN108441888A CN 108441888 A CN108441888 A CN 108441888A CN 201810460439 A CN201810460439 A CN 201810460439A CN 108441888 A CN108441888 A CN 108441888A
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CN
China
Prior art keywords
tin
electrolyte
compound additive
sulfonic acid
electrorefining
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CN201810460439.0A
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Chinese (zh)
Inventor
徐鹏翀
钟晓聪
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Jiangxi University of Science and Technology
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Jiangxi University of Science and Technology
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Priority to CN201810460439.0A priority Critical patent/CN108441888A/en
Publication of CN108441888A publication Critical patent/CN108441888A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C1/00Electrolytic production, recovery or refining of metals by electrolysis of solutions
    • C25C1/14Electrolytic production, recovery or refining of metals by electrolysis of solutions of tin

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The invention discloses a kind of tin electrorefining electrolyte compound additives, the compound additive group becomes chloride, sulphite and lignosulfonates, after being added to tin electrorefining electrolyte, 1 20 g/L of chloride concentration, 1 10 g/L of sulfite concentration, 2 10 g/L of lignin sulfonic acid salinity in electrolyte.The toluene phenol sulfonic acid of 20 ~ 40 g/L is generally added in traditional tin electrorefining electrolyte to inhibit Sn in electrolyte2+Oxidation, improve and electrolyte stability and improve cathode tin pattern.However cresol sulfonic acid smell is big, poisonous and harmful, deterioration potroom operating environment.Based on this, the present invention proposes a kind of green, efficient tin electrorefining electrolyte compound additive.The compound additive has the advantages that safe and non-toxic, at low cost, the raising smooth consistency of cathode tin, is easily promoted and applied in tin electrorefining industry.

Description

A kind of tin electrorefining electrolyte compound additive
Technical field
The invention belongs to non-ferrous metallurgy fields, are related to a kind of tin electrorefining electrolysis additive.
Background technology
Pyro-refining is compared, tin electrorefining has the advantages that work flow is short, cathode tin purity is high, is suitable for processing impurity The higher thick tin of content.In tin electrorefining processes, electrolyte composition is generally 20 ~ 40 g/L Sn2+、80~120 g/L H2SO4, 20 ~ 40 g/L cresol sulfonic acids, latex, betanaphthol etc..Due to Sn2+Sediment dynamics are fast, and cathode tin is easily in that dendritic crystalline is given birth to It is long, lead to that cathode tin burr is more, planarization is poor, is unfavorable for electrolysis operation.Cresol sulfonic acid has the work for making the smooth densification of cathode tin With tin electrolytic industry continues to use always cresol sulfonic acid.However, cresol sulfonic acid smell weight, poisonous and harmful, severe exacerbation operating environment. Seek a kind of novel tin electrorefining electrolysis additive to be of great significance to substitute cresol sulfonic acid.
Pertinent literature is reported and previous experiments are research shows that cresol sulfonic acid improves the mechanism of action master of tin cathode run Will there are three types of, first, phenolic hydroxyl group in cresol sulfonic acid molecule has reproducibility, inhibit Sn in electrolyte2+It is oxidized to Sn4+, in turn Reduce Sn (OH)4The generation of colloid slows down Sn (OH)4Colloid adheres in cathode and deteriorates cathode pattern;Second is that cresol sulfonic acid molecule In sulfonic group be adsorbed on cathode surface, block Sn2+Fast deposition, make the smooth densification of cathode tin;Third, cresol sulfonic acid has Complexing, with Sn2+Complex ion is formed, complex ion must be dissociated before complex ion deposition, sediment dynamics are slow, favorably In formation compacted cathode tin.The mechanism of action for improving tin cathode run according to cresol sulfonic acid proposes a kind of novel tin electrolysis Electrolyte compound additive is refined, group is as 1 ~ 20 g/L chlorides, 1 ~ 10 g/L sulphite, 2 ~ 10 g/L lignin sulfonic acids Salt.Wherein, the Cl that chloride provides-It can be as the complex ion of Sn (II);The SO that sulphite provides3 2-As reducing agent It can inhibit Sn2+Oxidation;Sulfonic group in lignosulfonates can play the role of blocking cathode tin deposition.Chloride, Sulphite and the compound addition of lignosulfonates, the phase of cathode tin densification flatness and addition cresol sulfonic acid electrolyte system When.In addition, the compound additive each component is cheap, safe and non-toxic, potroom smell can be greatly reduced, improve operation Environment.The compound additive has larger industrial application value, is easily promoted in tin electrolytic industry.
Invention content
, pollution workshop labourer heavy, poisonous and harmful for the cresol sulfonic acid smell that is added in traditional tin electrorefining electrolyte The problem of environment, the present invention propose a kind of environmentally friendly, efficient tin electrorefining electrolyte compound additive.
A kind of tin electrorefining electrolyte compound additive of the present invention, consisting of chloride, sulphite and Lignosulfonates, after being added to tin electrorefining electrolyte, chloride concentration 1-20 g/L, sulfite concentration in electrolyte 1-10 g/L, lignin sulfonic acid salinity 2-10 g/L.
Further, the chloride can be selected from HCl, NaCl, SnCl2, one or more of KCl, preferably HCl.
Further, the sulphite is selected from Na2SO3、K2SO3One or both of, preferably Na2SO3
Further, the lignosulfonates are selected from one or both of sodium lignin sulfonate, calcium lignosulfonate, Preferably sodium lignin sulfonate.
A kind of tin electrorefining electrolyte compound additive proposed by the present invention substitutes cresol sulfonic acid, can improve operation ring Border reduces cost, while maintaining the smooth densification of cathode tin, and there is important commercial introduction to be worth.
Specific implementation mode
Present disclosure is described in detail with the following Examples.
[comparative example 1]
Tin electrorefining electrolyte group becomes:95 g/L H2SO4,30 g/LSn2+ (are incorporated) with SnSO4,20 g/L toluene Phenol sulfonic acid, 2 g/L betanaphthols, 5 g/L latexes;Electrolyte temperature is 35 DEG C;100 A/m2 of current density;Potroom is natural Ventilation.After electrolysis 18 days, there is apparent phenols smell in workshop, and labourer's environment is poor, the smooth densification of cathode tin of output.
[comparative example 2]
Tin electrorefining electrolyte group becomes:95 g/L H2SO4,30 g/LSn2+ (are incorporated) with SnSO4,5 g/L cresols Sulfonic acid, 2 g/L betanaphthols, 5 g/L latexes;Electrolyte temperature is 35 DEG C;100 A/m2 of current density;Potroom is naturally logical Wind.After electrolysis 18 days, workshop has phenols smell, labourer's environment to make moderate progress compared with comparative example 1, the smooth cause of cathode tin of output Density is slightly below comparative example 1.
[embodiment 1]
Tin electrorefining electrolyte group becomes:95 g/L H2SO4,30 g/LSn2+ (are incorporated) with SnSO4,5 g/L HCl, and 5 G/L Na2SO3,5g/L sodium lignin sulfonates, 2 g/L betanaphthols, 5 g/L latexes;Electrolyte temperature is 35 DEG C;Electric current is close Spend 100 A/m2;Potroom gravity-flow ventilation.After electrolysis 18 days, without apparent smell, labourer's environment is good in workshop, the cathode tin of output Smooth consistency is slightly below comparative example 2.
[embodiment 2]
Tin electrorefining electrolyte group becomes:95 g/L H2SO4,30 g/LSn2+ (are incorporated) with SnSO4,15 g/L HCl, and 5 G/L Na2SO3,5g/L sodium lignin sulfonates, 2 g/L betanaphthols, 5 g/L latexes;Electrolyte temperature is 35 DEG C;Electric current is close Spend 100 A/m2;Potroom gravity-flow ventilation.After electrolysis 18 days, without apparent smell, labourer's environment is good in workshop, the cathode tin of output Smooth consistency is suitable with comparative example 2.
[embodiment 3]
Tin electrorefining electrolyte group becomes:95 g/L H2SO4,30 g/LSn2+ (are incorporated) with SnSO4,15 g/L HCl, and 5 G/L Na2SO3,10g/L sodium lignin sulfonates, 2 g/L betanaphthols, 5 g/L latexes;Electrolyte temperature is 35 DEG C;Electric current is close Spend 100 A/m2;Potroom gravity-flow ventilation.After electrolysis 18 days, without apparent smell, labourer's environment is good in workshop, the cathode tin of output Smooth consistency is suitable with comparative example 1.

Claims (4)

1. a kind of tin electrorefining electrolyte compound additive, which is characterized in that compound additive group becomes chloride, sulfurous acid Salt and lignosulfonates, after being added to tin electrorefining electrolyte, chloride concentration 1-20 g/L, sulfurous acid in electrolyte Salinity 1-10 g/L, lignin sulfonic acid salinity 2-10 g/L.
2. a kind of tin electrorefining electrolyte compound additive according to claim 1, which is characterized in that the chloride It can be selected from HCl, NaCl, SnCl2, one or more of KCl, preferably HCl.
3. a kind of tin electrorefining electrolyte compound additive according to claim 1, which is characterized in that the sulfurous acid Salt is selected from Na2SO3、K2SO3One or both of, preferably Na2SO3
4. a kind of tin electrorefining electrolyte compound additive according to claim 1, which is characterized in that the lignin Sulfonate is selected from one or both of sodium lignin sulfonate, calcium lignosulfonate, preferably sodium lignin sulfonate.
CN201810460439.0A 2018-05-15 2018-05-15 A kind of tin electrorefining electrolyte compound additive Pending CN108441888A (en)

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Publications (1)

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Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101260540A (en) * 2008-04-22 2008-09-10 云南驰宏锌锗股份有限公司 Composite additive for lead electrolysis
CN101892496A (en) * 2010-06-30 2010-11-24 四川鑫炬矿业资源开发股份有限公司 Method for preparing high-purity 5N tellurium from 3N crude tellurium
CN102534217A (en) * 2012-03-19 2012-07-04 赵芸 Tin dross reducing agent
CN102534661A (en) * 2012-01-19 2012-07-04 北京化工大学 Method for refining crude lead
CN103114303A (en) * 2013-03-08 2013-05-22 贵州遵义汇兴铁合金有限责任公司 Process method for deep purification in production for high-purity non-selenium electrolytic manganese metal and additive
CN103469248A (en) * 2013-09-23 2013-12-25 益阳金能新材料有限责任公司 Production method of electrolytic manganese metal
CN103540743A (en) * 2012-07-13 2014-01-29 张超 Hydrometallurgical method of metal sulfides
CN103540954A (en) * 2012-07-13 2014-01-29 张超 Metal electrolytic method in alkaline solutions
CN104562085A (en) * 2014-12-22 2015-04-29 芜湖金龙模具锻造有限责任公司 Crude lead electrolytic refining method
CN104746098A (en) * 2015-03-24 2015-07-01 昆明理工大学 Electrolyte and method for electrolyzing and refining crude lead
CN104789755A (en) * 2015-04-23 2015-07-22 中南大学 Method and device of utilizing high-sulfur manganese mine to cleanly and efficiently produce manganese metal
CN106399724A (en) * 2016-10-27 2017-02-15 中南大学 Microwave reduction roasting and extracting method for manganese oxide ore
CN107675209A (en) * 2017-10-18 2018-02-09 江西理工大学 A kind of green tin electrorefining electrolyte

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101260540A (en) * 2008-04-22 2008-09-10 云南驰宏锌锗股份有限公司 Composite additive for lead electrolysis
CN101892496A (en) * 2010-06-30 2010-11-24 四川鑫炬矿业资源开发股份有限公司 Method for preparing high-purity 5N tellurium from 3N crude tellurium
CN102534661A (en) * 2012-01-19 2012-07-04 北京化工大学 Method for refining crude lead
CN102534217A (en) * 2012-03-19 2012-07-04 赵芸 Tin dross reducing agent
CN103540743A (en) * 2012-07-13 2014-01-29 张超 Hydrometallurgical method of metal sulfides
CN103540954A (en) * 2012-07-13 2014-01-29 张超 Metal electrolytic method in alkaline solutions
CN103114303A (en) * 2013-03-08 2013-05-22 贵州遵义汇兴铁合金有限责任公司 Process method for deep purification in production for high-purity non-selenium electrolytic manganese metal and additive
CN103469248A (en) * 2013-09-23 2013-12-25 益阳金能新材料有限责任公司 Production method of electrolytic manganese metal
CN104562085A (en) * 2014-12-22 2015-04-29 芜湖金龙模具锻造有限责任公司 Crude lead electrolytic refining method
CN104746098A (en) * 2015-03-24 2015-07-01 昆明理工大学 Electrolyte and method for electrolyzing and refining crude lead
CN104789755A (en) * 2015-04-23 2015-07-22 中南大学 Method and device of utilizing high-sulfur manganese mine to cleanly and efficiently produce manganese metal
CN106399724A (en) * 2016-10-27 2017-02-15 中南大学 Microwave reduction roasting and extracting method for manganese oxide ore
CN107675209A (en) * 2017-10-18 2018-02-09 江西理工大学 A kind of green tin electrorefining electrolyte

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Application publication date: 20180824