CN108441888A - A kind of tin electrorefining electrolyte compound additive - Google Patents
A kind of tin electrorefining electrolyte compound additive Download PDFInfo
- 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
- Authority
- CN
- China
- Prior art keywords
- tin
- electrolyte
- compound additive
- sulfonic acid
- electrorefining
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
- C25C1/14—Electrolytic production, recovery or refining of metals by electrolysis of solutions of tin
Landscapes
- 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
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.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810460439.0A CN108441888A (en) | 2018-05-15 | 2018-05-15 | A kind of tin electrorefining electrolyte compound additive |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810460439.0A CN108441888A (en) | 2018-05-15 | 2018-05-15 | A kind of tin electrorefining electrolyte compound additive |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108441888A true CN108441888A (en) | 2018-08-24 |
Family
ID=63203719
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810460439.0A Pending CN108441888A (en) | 2018-05-15 | 2018-05-15 | A kind of tin electrorefining electrolyte compound additive |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108441888A (en) |
Citations (13)
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 |
-
2018
- 2018-05-15 CN CN201810460439.0A patent/CN108441888A/en active Pending
Patent Citations (13)
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 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
TWI425121B (en) | Process for plating chromium from a trivalent chromium plating bath | |
KR20070083922A (en) | Gold plating liquid and gold plating method | |
CN1880512A (en) | Trivalent chromium electroplating solution in sulfate system and method for preparing same | |
JP2009109007A (en) | Sliding element and its manufacturing method | |
WO2019119487A1 (en) | Hydroxyl graphene modified clad layer sealant and preparation method therefor | |
JP3306438B2 (en) | Alkoxylated dimercaptans as copper additives | |
CN108054403A (en) | The application of sodium alginate, magnesium-air cell electrolyte corrosion inhibitor, electrolyte and preparation method thereof, magnesium-air cell | |
CN107675212B (en) | A kind of Zinc electrolysis fluorine-resistant lead base composite anode and preparation method thereof | |
CN108441888A (en) | A kind of tin electrorefining electrolyte compound additive | |
CA1210733A (en) | Electrodeposition of chromium and its alloys | |
CA1209088A (en) | Electrodeposition of chromium and its alloys | |
CA1208159A (en) | Electrodeposition of chromium and its alloys | |
CN1643185A (en) | Gold plating solution and gold plating method | |
CN113215414B (en) | Method for removing magnesium in zinc hydrometallurgy process | |
JP4186716B2 (en) | Gold plating solution and gold plating method | |
CN107164794B (en) | Hard anodic oxidation electrolyte additive for air conditioner compressor aluminum alloy part | |
CN109457273A (en) | A kind of environmental type tin electrorefining electrolyte | |
TW201627540A (en) | High-purity copper electrolytic refining additive and method for producing high-purity copper | |
GB2141138A (en) | Trivalent chromium electroplating electrolytes and rejuvenation thereof | |
US2313338A (en) | Electrolytic zinc dust process | |
CN114292128B (en) | Solution for electrochemically repairing concrete cracks and preparation method thereof | |
CN114808039B (en) | Acid etching solution regeneration system without chlorine precipitation and low in cost | |
CN113463156B (en) | Magnesium hydroxide film layer and preparation method and system thereof | |
CN111170420B (en) | Method for removing fluorine ions in solution | |
US3098019A (en) | Electrolytic production of zinc |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
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: 20180824 |