CN100362130C - Method of chemical copper plating on hydregen storage alloy surface - Google Patents

Method of chemical copper plating on hydregen storage alloy surface Download PDF

Info

Publication number
CN100362130C
CN100362130C CNB2005101273384A CN200510127338A CN100362130C CN 100362130 C CN100362130 C CN 100362130C CN B2005101273384 A CNB2005101273384 A CN B2005101273384A CN 200510127338 A CN200510127338 A CN 200510127338A CN 100362130 C CN100362130 C CN 100362130C
Authority
CN
China
Prior art keywords
storage alloy
copper plating
hydrogen storage
chemical copper
alloy powder
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.)
Expired - Fee Related
Application number
CNB2005101273384A
Other languages
Chinese (zh)
Other versions
CN1786267A (en
Inventor
张森
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.)
Harbin Engineering University
Original Assignee
Harbin Engineering University
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 Harbin Engineering University filed Critical Harbin Engineering University
Priority to CNB2005101273384A priority Critical patent/CN100362130C/en
Publication of CN1786267A publication Critical patent/CN1786267A/en
Application granted granted Critical
Publication of CN100362130C publication Critical patent/CN100362130C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The present invention provides a method of a chemical copper plating process on a hydrogen storage alloy surface, which comprises the following steps: a screening process is carried out by a standard sample dividing screen, and uniform hydrogen storage alloy powder with the granularity of 300 to 400 meshes is selected; 0.9375 g to 4.6875 g of CuSO4.5H2O is dissolved in 200 ml of distillated water, 0.10 to 0.25 mL of HF is added, the temperature is controlled from 30 to 40 DEG C, and a stirring process is carried out; 12 g of hydrogen storage alloy powder is added into a reactor, the stirring speed is from 600 to 800 rpm by control, and a reaction is immediately stopped after the pH value of solution is stabilized to 3.5 to 3.3; hydrogen storing alloy is repetitively washed by the distillated water and anhydrous alcohol, and a product is obtained by drying in vacuum. The method of a chemical copper plating process on a hydrogen storage alloy surface has the advantages of high reaction speed, small environmental pollution, convenient operation, low cost, etc.

Description

A kind of method of chemical copper plating on hydregen storage alloy surface
Technical field
What the present invention relates to is a kind of surface treatment method of material, specifically a kind of method of chemical copper plating on hydregen storage alloy surface.
Background technology
The MH/Ni battery is a kind of high energy free of contamination " green energy resource ", has excellent specific properties such as specific energy height, specific power height, life-span length and security are good, is that the ideal of the used for electric vehicle power type energy is selected.Hydrogen storage alloy is the principal element that influences battery performance and cycle life as MH/Ni battery negative material commonly used, also is the major reason that limit cell performance improves.In order to improve the performance of hydrogen storage alloy, usually adopt the method that alloy surface is coated copper, as surface acidity copper facing, referring to F.Feng etc. at 2003 167 volumes of international publication " Surface and Coating Technology " 263-268 publish thesis " Improved performance of a metal hydride electrode for nickel/metalhydride batteries through copper-coating ", alkaline copper plating is referring to magnifying to waiting at " power technology " 1998 22 volumes 3 phase 111-114 publish thesis " about several problems of the surperficial copper-clad technology of hydrogen storage alloy ".But these methods all exist cost height, complex process, long flow path, toxicity greatly, problem such as not easy to operate and control.Therefore, require further improvement the copper coating method, improve copper-plated time and efficient.
Summary of the invention
It is short to the purpose of this invention is to provide a kind of operating time, copper facing efficient height, and cost is low, and flow process is simple and can reduce the method for chemical copper plating on hydregen storage alloy surface of environmental pollution.
The object of the present invention is achieved like this: with the screening of standard sub-sieve, choose granularity uniform hydrogen storing alloy powder between 300~400 orders; With 0.9375g~4.6875g CuSO 45H 2O is dissolved in the 200ml distilled water, adds the HF of 0.10~0.25mL, and controlled temperature is at 30~40 ℃, and the control stirring velocity is 600~800rpm; The 12g hydrogen storing alloy powder is added in the reactor, and the control stirring velocity is 600~800rpm, treats behind solution PH value stabilization to 3.3~3.5 stopped reaction immediately; Clean hydrogen storage alloy repeatedly with distilled water and dehydrated alcohol, vacuum drying obtains product.Wherein, used hydrogen storing alloy powder is AB 5Or AB 2Type.
The invention has the advantages that: 1, speed of response is fast, and whole copper facing whole process is approximately 1~2 minute.2, copper facing efficient height after reaction finishes, does not have cupric ion again and exists in the solution, illustrate that copper facing efficient is near 100%.3, environmental pollution is little, does not have toxic substance in the reaction process, and reaction finishes, and no cupric ion exists in the solution of back.4, easy to operate, entire reaction course only need be carried out under stirring condition, does not need to control complicated parameter, and it is very easy to operate.5, cost is low, and whole process does not need expensive raw material, does not have big energy expenditure, does not need big equipment input.
Embodiment
For example the present invention is done in more detail below and describes:
With the screening of standard sub-sieve, choose granularity uniform AB between 300~400 orders 5Type (La13.25wt.%, Ni 69.37wt.%, Co 7.14wt.%, Mn 4.86wt.%, Ce 3.15wt.%) hydrogen storing alloy powder; With 0.9375g CuSO 45H 2O is dissolved in the 200ml distilled water, adds the HF of 0.10mL, and controlled temperature is at 30 ℃, and the control stirring velocity is 600rpm; The 12g hydrogen storing alloy powder is added in the reactor, and the control stirring velocity is 600rpm, treats solution PH value stabilization to 3.3 stopped reaction immediately; Clean hydrogen storage alloy repeatedly with distilled water and dehydrated alcohol, vacuum drying obtains product.
With the screening of standard sub-sieve, choose granularity uniform AB between 300~400 orders 5Type (La13.25wt.%, Ni 69.37wt.%, Co 7.14wt.%, Mn 4.86wt.%, Ce 3.15wt.%) hydrogen storing alloy powder; With 4.6875g CuSO 45H 2O is dissolved in the 200ml distilled water, adds the HF of 0.20mL, and controlled temperature is at 35 ℃, and the control stirring velocity is 600rpm; The 12g hydrogen storing alloy powder is added in the reactor, and the control stirring velocity is 600rpm, treats solution PH value stabilization to 3.4 stopped reaction immediately; Clean hydrogen storage alloy repeatedly with distilled water and dehydrated alcohol, vacuum drying obtains product.
With the screening of standard sub-sieve, choose granularity uniform AB between 300~400 orders 5Type (La13.25wt.%, Ni 69.37wt.%, Co 7.14wt.%, Mn 4.86wt.%, Ce 3.15wt.%) hydrogen storing alloy powder; With 2.6875g CuSO 45H 2O is dissolved in the 200ml distilled water, adds the HF of 0.25mL, and controlled temperature is at 40 ℃, and the control stirring velocity is that 600rpm adds the 12g hydrogen storing alloy powder in the reactor, and the control stirring velocity is 600rpm, treats solution PH value stabilization to 3.5 stopped reaction immediately; Clean hydrogen storage alloy repeatedly with distilled water and dehydrated alcohol, vacuum drying obtains product.
The invention has the advantages that: 1, speed of response is fast, and whole copper facing whole process is approximately 1~2 minute.2, copper facing efficient height after reaction finishes, does not have cupric ion again and exists in the solution, illustrate that copper facing efficient is near 100%.3, environmental pollution is little, does not have toxic substance in the reaction process, and reaction finishes, and no cupric ion exists in the solution of back.4, easy to operate, entire reaction course only need be carried out under stirring condition, does not need to control complicated parameter, and it is very easy to operate.5, cost is low, and whole process does not need expensive raw material, does not have big energy expenditure, does not need big equipment input.
The applied scope of the present invention is: AB 5Or AB 2The type hydrogen storage alloy powder.

Claims (2)

1. method of chemical copper plating on hydregen storage alloy surface is characterized in that: this method is with the screening of standard sub-sieve, chooses granularity hydrogen storing alloy powder uniformly between 300~400 orders; With 0.9375g~4.6875gCuSO 45H 2O is dissolved in the 200ml distilled water, adds the HF of 0.10~0.25mL, and controlled temperature stirs at 30~40 ℃; The 12g hydrogen storing alloy powder is added in the reactor, stir, treat behind solution PH value stabilization to 3.3~3.5 stopped reaction immediately; Clean hydrogen storage alloy repeatedly with distilled water and dehydrated alcohol, vacuum drying obtains product; Wherein, hydrogen storing alloy powder is AB 5Or AB 2Type.
2. method of chemical copper plating on hydregen storage alloy surface according to claim 1, it is characterized in that: stirring velocity is controlled at 600~800rpm.
CNB2005101273384A 2005-12-15 2005-12-15 Method of chemical copper plating on hydregen storage alloy surface Expired - Fee Related CN100362130C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNB2005101273384A CN100362130C (en) 2005-12-15 2005-12-15 Method of chemical copper plating on hydregen storage alloy surface

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNB2005101273384A CN100362130C (en) 2005-12-15 2005-12-15 Method of chemical copper plating on hydregen storage alloy surface

Publications (2)

Publication Number Publication Date
CN1786267A CN1786267A (en) 2006-06-14
CN100362130C true CN100362130C (en) 2008-01-16

Family

ID=36783879

Family Applications (1)

Application Number Title Priority Date Filing Date
CNB2005101273384A Expired - Fee Related CN100362130C (en) 2005-12-15 2005-12-15 Method of chemical copper plating on hydregen storage alloy surface

Country Status (1)

Country Link
CN (1) CN100362130C (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103203452A (en) * 2013-03-28 2013-07-17 桂林理工大学 Method of surface copper plating modification for AB3 type hydrogen storage alloy

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1119791A (en) * 1994-09-30 1996-04-03 北京科技大学 Cheap rare-earth hydrogen storage electrode alloy containing copper and low cobalt
JPH1170942A (en) * 1997-08-28 1999-03-16 Showa Alum Corp Sealed container with internal partition
CN1316537A (en) * 2001-03-23 2001-10-10 天津南开戈德集团有限公司 Mg-base hydrogen-bearing alloy material and its preparing process and application
KR20010090630A (en) * 2000-04-10 2001-10-19 김민수 The method of hydrogen storck useing lanthanum-nickel alloy
CN1424433A (en) * 2003-01-14 2003-06-18 南开大学 Chemical coppering process for non-aqueous system hydrogen storage alloy powder
CN1601172A (en) * 2004-10-16 2005-03-30 浙江大学 Storage device for hydrogen

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1119791A (en) * 1994-09-30 1996-04-03 北京科技大学 Cheap rare-earth hydrogen storage electrode alloy containing copper and low cobalt
JPH1170942A (en) * 1997-08-28 1999-03-16 Showa Alum Corp Sealed container with internal partition
KR20010090630A (en) * 2000-04-10 2001-10-19 김민수 The method of hydrogen storck useing lanthanum-nickel alloy
CN1316537A (en) * 2001-03-23 2001-10-10 天津南开戈德集团有限公司 Mg-base hydrogen-bearing alloy material and its preparing process and application
CN1424433A (en) * 2003-01-14 2003-06-18 南开大学 Chemical coppering process for non-aqueous system hydrogen storage alloy powder
CN1601172A (en) * 2004-10-16 2005-03-30 浙江大学 Storage device for hydrogen

Also Published As

Publication number Publication date
CN1786267A (en) 2006-06-14

Similar Documents

Publication Publication Date Title
Xiao et al. Novel approach for in situ recovery of lithium carbonate from spent lithium ion batteries using vacuum metallurgy
Qu et al. Recovery of LiCoO2 from spent lithium-ion batteries through a low-temperature ammonium chloride roasting approach: thermodynamics and reaction mechanisms
Yao et al. Hydrometallurgical processes for recycling spent lithium-ion batteries: a critical review
Tang et al. Recovery and regeneration of LiCoO2-based spent lithium-ion batteries by a carbothermic reduction vacuum pyrolysis approach: Controlling the recovery of CoO or Co
Bertheussen et al. Electroreduction of CO on polycrystalline copper at low overpotentials
Fan et al. Leaching mechanisms of recycling valuable metals from spent lithium-ion batteries by a malonic acid-based leaching system
Doo et al. Hydrophobic Ni-rich layered oxides as cathode materials for lithium-ion batteries
Park et al. Recent advances in rechargeable magnesium battery technology: a review of the field’s current status and prospects
Wang et al. Selective extraction of critical metals from spent lithium-ion batteries
Park et al. Exploiting the steric effect and low dielectric constant of 1, 2-dimethoxypropane for 4.3 V lithium metal batteries
JP2022510241A (en) Methods and systems for expandable direct recycling of batteries
US9676034B2 (en) Method of manufacturing powder having high surface area
McKay et al. CoCrFeNi high-entropy alloy as an enhanced hydrogen evolution catalyst in an acidic solution
Ferrara et al. Circular economy and the fate of lithium batteries: second life and recycling
Liu et al. Synthesis of Ni-rich cathode material from maleic acid-leachate of spent lithium-ion batteries
CN107460503A (en) The method that micro-nano copper powder is reclaimed from waste printed circuit board
Akhmetov et al. Li-Ion Battery Cathode Recycling: An Emerging Response to Growing Metal Demand and Accumulating Battery Waste
Kim et al. Exploring optimal water splitting bifunctional alloy catalyst by pareto active learning
Hua et al. Efficient separation of electrode active materials and current collector metal foils from spent lithium-ion batteries by a green deep eutectic solvent
CN100362130C (en) Method of chemical copper plating on hydregen storage alloy surface
Xu et al. Creative method for efficiently leaching Ni, Co, Mn, and Li in a mixture of LiFePO4 and LiMO2 using only Fe (III)
Ma et al. An efficient and precipitant-free approach to selectively recover lithium cobalt oxide made for cathode materials using a microwave-assisted deep eutectic solvent
Yang et al. Optimization of the zinc oxide reduction in the charging process of zinc‐air flow batteries
Zhan et al. Recycling zinc and preparing high-value-added nanozinc oxide from waste zinc–manganese batteries by high-temperature evaporation-separation and oxygen control oxidation
Vieceli et al. Recycling of lithium-ion batteries: Effect of hydrogen peroxide and a dosing method on the leaching of LCO, NMC oxides, and industrial black mass

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20080116

Termination date: 20101215