CN106854768B - electrodeposition preparation method of superfine copper powder - Google Patents

electrodeposition preparation method of superfine copper powder Download PDF

Info

Publication number
CN106854768B
CN106854768B CN201611022171.XA CN201611022171A CN106854768B CN 106854768 B CN106854768 B CN 106854768B CN 201611022171 A CN201611022171 A CN 201611022171A CN 106854768 B CN106854768 B CN 106854768B
Authority
CN
China
Prior art keywords
copper
copper powder
powder
electrodeposition
superfine
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.)
Active
Application number
CN201611022171.XA
Other languages
Chinese (zh)
Other versions
CN106854768A (en
Inventor
李贵
李彦龙
马琳亭
崔海瑞
纪武仁
赵宏
易超
曹桂银
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.)
Northwest Research Institute of Mining and Metallurgy
Original Assignee
Northwest Research Institute of Mining and Metallurgy
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 Northwest Research Institute of Mining and Metallurgy filed Critical Northwest Research Institute of Mining and Metallurgy
Priority to CN201611022171.XA priority Critical patent/CN106854768B/en
Publication of CN106854768A publication Critical patent/CN106854768A/en
Application granted granted Critical
Publication of CN106854768B publication Critical patent/CN106854768B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C5/00Electrolytic production, recovery or refining of metal powders or porous metal masses
    • C25C5/02Electrolytic production, recovery or refining of metal powders or porous metal masses from solutions

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 an electrodeposition preparation method of superfine copper powder. The method comprises the steps of preparing a copper sulfate solution by taking industrial copper sulfate as a raw material, adding concentrated ammonia water, sulfuric acid and a dispersing agent to stabilize copper ions, changing the precipitation potential of copper, increasing the reaction force among solid particles, then performing electrodeposition to stably precipitate the copper to obtain copper powder, finally washing the copper powder, placing the washed copper powder in an antioxidant solution, stirring at room temperature to perform surface modification, then washing and drying to obtain the superfine copper powder with stable properties. The invention takes industrial copper sulfate as raw material, so the cost is lower and the raw material source is wider; copper ions can be uniformly separated out at the cathode, and superfine copper powder with small, uniform and narrow distribution grain size is obtained, wherein the median grain size is about 0.925 mu m, and the superfine copper powder can be placed in the air for more than 150 days without being oxidized.

Description

The electrodeposition preparation method of superfine cupper powder
Technical field
It is specifically a kind of using industrial cupric sulfate to be raw material, ultra-fine the present invention relates to a kind of preparation method of metal powder The electrodeposition preparation method of copper powder.
Background technique
With the development of industrial technology, submicron particle is increasingly becoming emerging high-tech product and sophisticated industry basis material Material.Superfine cupper powder becomes the base that purposes is wide, potentiality are big, economic value added is high due to the characteristics such as its intensity is high, conducts electricity very well Plinth functional powder material is widely used in the bath of the necks such as metallurgy, electronics, medicine and machinery.
Copper powder particle size and inoxidizability are the main indicator of gauge copper mealiness energy, and influence the main of copper powder price Factor.Currently, more mature copper powder preparation method has atomization, chemical reduction method and electrolysis method.Atomization and electronation Method, for raw material, keeps production cost high dependent on cathode copper or with fine copper etc.;Electrolysis method generally uses fine copper plate to do anode, Titanium plate does cathode, and sulfate system does electrolyte, and the anode scrap after electrolysis need to constantly replace and founding again, the copper powder of generation Grain is larger, and micron order is not achieved, and size distribution is uneven, it is serious to reunite, and leads to entire production technology large labor intensity, cost Height, obtained copper powder economic value added are low.Application No. is 200510007317.9 Chinese invention patents to provide a kind of electrodeposition The method of production copper powder expands the raw material sources of copper powder, fundamentally reduces copper using copper sponge or copper scap as raw material The production cost of powder, but copper powder size made from this method is still larger, up to 70 μm or so, and its antioxygenic property also without Method is protected, and causes its economic value added still lower.
Summary of the invention
The object of the present invention is to provide a kind of low production cost, copper powder particle size is small and is evenly distributed, copper powder inoxidizability The electrodeposition preparation method of superfine cupper powder that can be high, to further increase the economic value added of copper powder.
The purpose of the present invention is what is realized by following scheme: using industrial cupric sulfate as raw material, configuring copper-bath, so Concentrated ammonia liquor, sulfuric acid and dispersing agent are added afterwards and stablizes copper ion, changes the deposition potential of copper, increase the reaction force between solid particle After carry out electrodeposition, make copper stablize be precipitated obtain copper powder, finally by copper powder washing be placed in antioxidant solution, stir at room temperature Carry out that surface is modified washes, is dried in vacuo again, to obtain superfine cupper powder.Specifically includes the following steps:
(1) configuration of electrolytic cell
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 4-5 cm;
(2) preparation of copper-containing solution
Using industrial cupric sulfate as raw material, it is configured to the copper-bath that copper ion concentration is 90-150 g/L and filtering;It takes Complexing agent, sulfuric acid and dispersing agent is added in filtrate, be configured to copper ion concentration be 5-40 g/L, ammonia concn be 80-160 g/L, The solution that sulfuric acid concentration is 60-200 g/L, dispersion dosage is 0.01-3%, heating water bath is to being pumped into electrolytic cell after 30-60 DEG C;
(3) the electrodeposition preparation of copper powder
It is passed through direct current, controls cathode-current density 600-2500 A/m2;In electrolytic deposition process, followed using peristaltic pump The feed liquor of ring liquid and out hydraulic control system, and the copper-bath that copper ion concentration is 90-150 g/L is added into circulation fluid, with The stabilization of electrodeposition environment is maintained, additional amount is the 1-5% of global cycle liquid product per hour;
(4) powder operation is scraped
In electrolytic deposition process, every 5-8 min progress once scrapes powder operation, to reduce the partial size of copper powder;
(5) copper powder anti-oxidant treatment
After electrodeposition operation, extracts liquid after electrodeposition out, copper powder is washed with deionized to neutrality residual in copper powder thoroughly to remove The electrolyte ion stayed is placed in the ethanol solution of antioxidant, and it is modified to carry out surface by stirring at room temperature;Change After copper powder after property is washed with deionized again, vacuum drying.
Dispersing agent is polyvinyl alcohol, triethanolamine or polyvinylpyrrolidone in above-mentioned steps (2).
Antioxidant is lauryl mercaptan or odium stearate, mass fraction 0.1-0.5% in step (5);Whip modified turns Speed is 100-300 r/min, and the time is 15-30 min;Modified, copper powder after washing drying pressure is 0.05-0.1 Mpa, is done Dry temperature is 40-70 DEG C.
Compared with prior art, the invention has the following advantages:
(1) the electrodeposition preparation method of superfine cupper powder of the present invention is using industrial cupric sulfate as raw material, and cost is lower, raw material sources It is more extensive.
(2) present invention makes Cu by the way that ammonium hydroxide is added into copper-bath2+Relatively stable [Cu is generated with complexing (NH3)4]2+, change Cu2+Copper ion is precipitated uniformly in cathode in deposition potential on cathode, and it is smaller, equal to obtain partial size Even and narrow distribution superfine cupper powder.
(3) it is about 0.925 μm using the superfine cupper powder median of method preparation in the present invention, can places in air 150 days or more and it is not oxidized, property stablize.
Detailed description of the invention
Fig. 1 is the superfine cupper powder particle size distribution figure of method preparation in the embodiment of the present invention 1.
In figure, abscissa indicates that partial size, ordinate indicate particle diameter distribution, and curve a is calculus cloth curve, and curve b is tired Count distribution curve.
Specific embodiment
For a better understanding of the present invention, the present invention will be further explained below with reference to the attached drawings and specific examples.
Embodiment 1
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 4 cm;With Industrial cupric sulfate is raw material, is configured to the copper-bath that copper ion concentration is 90 g/L and filtering;Take filtrate be added concentrated ammonia liquor, Sulfuric acid and polyvinyl alcohol, are configured to that copper ion concentration is 5 g/L, ammonia concn is 80 g/L, sulfuric acid concentration is 60 g/L, poly- second The solution that enol amount is 0.01%, heating water bath is to being pumped into electrolytic cell after 30 DEG C;It is passed through direct current, controls cathode-current density For 600 A/m2;In electrolytic deposition process, the feed liquor and hydraulic control system out of circulation fluid are carried out using peristaltic pump, and add into circulation fluid Copper ion concentration is the copper-bath of 90 g/L, and to maintain the stabilization of electrodeposition environment, additional amount is global cycle liquid per hour Long-pending 5%;In electrolytic deposition process, every 5 min progress once scrapes powder operation, to reduce the partial size of copper powder;After electrodeposition operation, extraction electricity Liquid after product copper powder is washed with deionized to neutrality thoroughly to remove remaining electrolyte ion in copper powder and be placed on quality point In lauryl mercaptan-ethanol solution that number is 0.1%, it is modified that 15 min progress surface is stirred with 100 r/min at room temperature; Modified copper powder be washed with deionized again after in 0.1 Mpa of pressure, temperature is to be dried in vacuo at 65 DEG C.
Granularmetric analysis shows that the copper powder size prepared using the above method is smaller, is evenly distributed and narrow, median D50= 0.877 μm (curve a, b in Fig. 1).
Stability test in air at room temperature shows that copper powder property in 155 days is stablized.
Embodiment 2
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 4 cm;With Industrial cupric sulfate is raw material, is configured to the copper-bath that copper ion concentration is 120 g/L and filtering;Take filtrate that dense ammonia is added Water, sulfuric acid and polyvinyl alcohol, are configured to that copper ion concentration is 10 g/L, ammonia concn is 100 g/L, sulfuric acid concentration is 80 g/ L, the solution that polyvinyl alcohol amount is 3%, heating water bath is to being pumped into electrolytic cell after 40 DEG C;It is passed through direct current, control cathode current is close Degree is 1800 A/m2;In electrolytic deposition process, the feed liquor and hydraulic control system out of circulation fluid are carried out using peristaltic pump, and into circulation fluid The copper-bath that copper ion concentration is 100 g/L is added, to maintain the stabilization of electrodeposition environment, additional amount is global cycle per hour The 4% of liquid product;In electrolytic deposition process, every 5 min progress once scrapes powder operation, to reduce the partial size of copper powder;After electrodeposition operation, take out Copper powder is washed with deionized to neutrality and is placed on matter thoroughly to remove remaining electrolyte ion in copper powder by liquid after electrodeposition out It measures in lauryl mercaptan-ethanol solution that score is 0.5%, stirs 20 min at room temperature with 300 r/min and carry out surface It is modified;Modified copper powder be washed with deionized again after in 0.05 Mpa of pressure, temperature is to be dried in vacuo at 40 DEG C.
Granularmetric analysis shows that the copper powder size prepared using the above method is smaller, is evenly distributed and narrow, median D50= 0.882 μm。
Stability test in air at room temperature shows that copper powder property in 160 days is stablized.
Embodiment 3
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 4.5 cm; Using industrial cupric sulfate as raw material, it is configured to the copper-bath that copper ion concentration is 120 g/L and filtering;Take filtrate that dense ammonia is added Water, sulfuric acid and triethanolamine, are configured to that copper ion concentration is 15 g/L, ammonia concn is 120 g/L, sulfuric acid concentration is 120 g/ L, the solution that triethanolamine amount is 0.05%, heating water bath is to being pumped into electrolytic cell after 40 DEG C;It is passed through direct current, control cathode electricity Current density is 1600 A/m2;In electrolytic deposition process, the feed liquor and hydraulic control system out of circulation fluid are carried out using peristaltic pump, and to circulation The copper-bath that copper ion concentration is 120 g/L is added in liquid, to maintain the stabilization of electrodeposition environment, additional amount is total per hour The 3% of circulation fluid volume;In electrolytic deposition process, every 5 min progress once scrapes powder operation, to reduce the partial size of copper powder;Electrodeposition operation Afterwards, liquid after extraction electrodeposition, copper powder is washed with deionized to neutrality thoroughly to remove in copper powder after remaining electrolyte ion Being placed in concentration is in odium stearate-ethanol solution that mass fraction is 0.1%, at room temperature with 200 r/min stirring 30 It is modified that min carries out surface;Modified copper powder be washed with deionized again after in 0.08 Mpa, temperature is vacuum at 55 DEG C It is dry.
Granularmetric analysis shows that the copper powder size prepared using the above method is smaller, is evenly distributed and narrow, median D50= 0.925 μm。
Stability test in air at room temperature shows that copper powder property in 170 days is stablized.
Embodiment 4
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 5 cm;With Industrial cupric sulfate is raw material, is configured to the copper-bath that copper ion concentration is 150 g/L and filtering;Take filtrate that dense ammonia is added Water, sulfuric acid and polyvinylpyrrolidone, are configured to that copper ion concentration is 30 g/L, ammonia concn is 150 g/L, sulfuric acid concentration is 150 g/L, the solution that polyvinylpyrrolidone amount is 1.5%, heating water bath is to being pumped into electrolytic cell after 50 DEG C;It is passed through direct current Electricity, control cathode-current density are 2200 A/m2;The feed liquor that circulation fluid is carried out using peristaltic pump in electrolytic deposition process and hydraulic control out System, and the copper-bath that copper ion concentration is 150 g/L is added into circulation fluid, to maintain the stabilization of electrodeposition environment, often Hour additional amount is the 2% of global cycle liquid product;In electrolytic deposition process, every 6 min progress once scrapes powder operation, to reduce copper powder Partial size;After electrodeposition operation, extracts liquid after electrodeposition out, copper powder is washed with deionized to neutrality remaining in copper powder thoroughly to remove Electrolyte ion is placed in odium stearate-ethanol solution that mass fraction is 0.5%, at room temperature with 300 r/min It is modified to stir 15 min progress surface;Modified copper powder be washed with deionized again after in 0.1 Mpa, temperature is at 45 DEG C Vacuum drying.
Granularmetric analysis shows that the copper powder size prepared using the above method is smaller, is evenly distributed and narrow, median D50= 0.952 μm。
Stability test in air at room temperature shows that copper powder property in 170 days is stablized.
Embodiment 5
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 5 cm;With Industrial cupric sulfate is raw material, is configured to the copper-bath that copper ion concentration is 150 g/L and filtering;Take filtrate that dense ammonia is added Water, sulfuric acid and polyvinylpyrrolidone, are configured to that copper ion concentration is 40 g/L, ammonia concn is 160 g/L, sulfuric acid concentration is 200 g/L, the solution that polyvinylpyrrolidone amount is 3%, heating water bath is to being pumped into electrolytic cell after 60 DEG C;It is passed through direct current, is controlled Cathode-current density processed is 2500 A/m2;In electrolytic deposition process, the feed liquor and hydraulic control system out of circulation fluid are carried out using peristaltic pump, with And added into circulation fluid copper ion concentration be 150 g/L copper-bath, to maintain the stabilization of electrodeposition environment, per hour plus Enter 1% that amount is global cycle liquid product;In electrolytic deposition process, every 8 min progress once scrapes powder operation, to reduce the partial size of copper powder;Electricity After product operation, extracts liquid after electrodeposition out, copper powder is washed with deionized to neutrality thoroughly to remove remaining electrolyte in copper powder Ion is placed in odium stearate-ethanol solution that mass fraction is 0.25%, at room temperature with 100 r/min stirring 30 It is modified that min carries out surface;Modified copper powder be washed with deionized again after in 0.05 Mpa, temperature is that vacuum is dry at 70 DEG C It is dry.
Granularmetric analysis shows that the copper powder size prepared using the above method is smaller, is evenly distributed and narrow, median D50= 0.987 μm。
Stability test in air at room temperature shows that copper powder property in 175 days is stablized.

Claims (3)

1. the electrodeposition preparation method of superfine cupper powder, which comprises the following steps:
(1) configuration of electrolytic cell
Make glass fibre electrolytic cell by oneself, using Pb-Ca-Sn alloy sheets as anode, pure copper sheet is cathode, and pole span is 4-5 cm;
(2) preparation of copper-containing solution
Using industrial cupric sulfate as raw material, it is configured to the copper-bath that copper ion concentration is 90-150 g/L and filtering;Take filtrate Concentrated ammonia liquor, sulfuric acid and dispersing agent is added, is configured to that copper ion concentration is 5-40 g/L, ammonia concn is 80-160 g/L, sulfuric acid The solution that concentration is 60-200 g/L, dispersion dosage is 0.01-3%, heating water bath is to being pumped into electrolytic cell after 30-60 DEG C;
(3) the electrodeposition preparation of copper powder
It is passed through direct current, controls cathode-current density 600-2500 A/m2;In electrolytic deposition process, circulation fluid is carried out using peristaltic pump Feed liquor and out hydraulic control system, and add into circulation fluid the copper-bath that copper ion concentration is 90-150 g/L, per hour plus Enter the 1-5% that amount is global cycle liquid product;
(4) powder operation is scraped
In electrolytic deposition process, every 5-8 min carries out once scraping powder operation;
(5) copper powder anti-oxidant treatment
After electrodeposition operation, liquid after electrodeposition is extracted out, it is 0.1- that copper powder, which is washed with deionized, and is placed on mass fraction to neutrality In the ethanol solution of 0.5% lauryl mercaptan, surface is carried out by stirring at room temperature and is modified, the revolving speed of whip modified is 100-300 r/min, time are 15-30 min;After modified copper powder is washed with deionized again, vacuum drying.
2. the electrodeposition preparation method of superfine cupper powder according to claim 1, it is characterised in that: disperse described in step (2) Agent is polyvinyl alcohol, triethanolamine or polyvinylpyrrolidone.
3. the electrodeposition preparation method of superfine cupper powder according to claim 1, it is characterised in that: modified described in step (5), The drying pressure of copper powder is 0.05-0.09 Mpa after washing, and temperature is 40-70 DEG C.
CN201611022171.XA 2016-11-21 2016-11-21 electrodeposition preparation method of superfine copper powder Active CN106854768B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611022171.XA CN106854768B (en) 2016-11-21 2016-11-21 electrodeposition preparation method of superfine copper powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611022171.XA CN106854768B (en) 2016-11-21 2016-11-21 electrodeposition preparation method of superfine copper powder

Publications (2)

Publication Number Publication Date
CN106854768A CN106854768A (en) 2017-06-16
CN106854768B true CN106854768B (en) 2019-03-26

Family

ID=59126316

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611022171.XA Active CN106854768B (en) 2016-11-21 2016-11-21 electrodeposition preparation method of superfine copper powder

Country Status (1)

Country Link
CN (1) CN106854768B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110144604B (en) * 2019-06-17 2020-06-09 阳谷祥光铜业有限公司 Preparation process of electrodeposited copper powder
CN110697756A (en) * 2019-10-26 2020-01-17 韩亚半导体材料(贵溪)有限公司 Production process of high-purity copper oxide powder for integrated circuit

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001181885A (en) * 1999-12-20 2001-07-03 Sumitomo Metal Mining Co Ltd Method for producing electrolytic metal powder
CN101024252A (en) * 2006-02-20 2007-08-29 培尔梅烈克电极股份有限公司 Production method for electrolyzing metal powder
CN101818364A (en) * 2009-04-03 2010-09-01 兰州理工大学 Method for preparing nano copper powder
CN102174700A (en) * 2011-03-02 2011-09-07 哈尔滨六环涂料化工有限公司 Copper powder antioxidant
CN102764898A (en) * 2012-08-09 2012-11-07 深圳市圣龙特电子有限公司 method for preparing ultrafine copper powder for electronic paste
CN102978667A (en) * 2012-10-25 2013-03-20 烟台大学 Preparation method for nanometer copper powder through electro-deposition
CN103388160A (en) * 2013-07-19 2013-11-13 北京科技大学 Method for preparation of ultrafine copper powder by waste circuit board copper dissolution-electrodeposition combined method
CN103397349A (en) * 2013-08-09 2013-11-20 北京科技大学 Preparation method of two-dimensional feathery copper powder under ammonia condition

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100344795C (en) * 2005-02-06 2007-10-24 金川集团有限公司 Method for producing copper powder by electrodeposition

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001181885A (en) * 1999-12-20 2001-07-03 Sumitomo Metal Mining Co Ltd Method for producing electrolytic metal powder
CN101024252A (en) * 2006-02-20 2007-08-29 培尔梅烈克电极股份有限公司 Production method for electrolyzing metal powder
CN101818364A (en) * 2009-04-03 2010-09-01 兰州理工大学 Method for preparing nano copper powder
CN102174700A (en) * 2011-03-02 2011-09-07 哈尔滨六环涂料化工有限公司 Copper powder antioxidant
CN102764898A (en) * 2012-08-09 2012-11-07 深圳市圣龙特电子有限公司 method for preparing ultrafine copper powder for electronic paste
CN102978667A (en) * 2012-10-25 2013-03-20 烟台大学 Preparation method for nanometer copper powder through electro-deposition
CN103388160A (en) * 2013-07-19 2013-11-13 北京科技大学 Method for preparation of ultrafine copper powder by waste circuit board copper dissolution-electrodeposition combined method
CN103397349A (en) * 2013-08-09 2013-11-20 北京科技大学 Preparation method of two-dimensional feathery copper powder under ammonia condition

Also Published As

Publication number Publication date
CN106854768A (en) 2017-06-16

Similar Documents

Publication Publication Date Title
CN103658637B (en) A kind of method of electrolytic preparation dendroid fine copper powder
CN103388160A (en) Method for preparation of ultrafine copper powder by waste circuit board copper dissolution-electrodeposition combined method
CN105220181A (en) From waste and old circuit board, the technique of copper for high pure and ultra-fine copper powder is reclaimed based on electrochemical process
CN106149026A (en) The preparation of a kind of Graphene/golden nanometer particle composite and characterizing method
CN106854768B (en) electrodeposition preparation method of superfine copper powder
CN102912375B (en) Method and the special purpose device thereof of copper is reclaimed from acidic etching liquid
CN107675199A (en) The technique that a kind of electrolysis prepares nickel sulfate
CN105328182B (en) A kind of preparation method of nucleocapsid structure silver copper-clad nano-powder material
CN104741622B (en) The preparation method of a kind of high pure copper powder
CN105648232B (en) One kind uses I2The method that gold refining is carried out with KI
CN109537030B (en) Preparation method of carbon nanoparticle solution and application of carbon nanoparticle solution in nickel coating
CN105441974A (en) Method for producing electrodeposited nickel
CN1932083A (en) Silver electrolyzing process
CN101333673B (en) Electrolytic solution for preparing nano ceramic coatings by micro-arc oxidation
CN107059065A (en) The additive package of electrolytic acid etching waste liquor and the method that copper powder is prepared with it
CN103938229B (en) Method for preparing ultrafine flake zinc powder by adding antimony compound alkali liquor to electrolyze
CN106987869B (en) The method for being electrolysed the additive package of alkaline etching waste liquid for producing and preparing copper powder with it
CN109234767B (en) Preparation method of superfine spherical copper powder
CN105838900B (en) One kind uses I2The method that gold refining is carried out with NaI
CN112410828A (en) Process for preparing high-purity silver by high-concentration silver nitrate electrodeposition method
CN204779868U (en) Many metal separation of centrifugation electrodeposition and purification system
CN107723748B (en) Application of the hollow plasma electrode of normal pressure in molten-salt electrolysis
CN103361700A (en) Electrolytic coloring method for aluminum sections
CN109809502A (en) A method of nickel sulfate is produced using electro deposited nickel anolyte
CN103866352A (en) Producing method of electrolytic copper powder

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
GR01 Patent grant
GR01 Patent grant