CN107069042A - A kind of lead-acid accumulator light-type grid and preparation method thereof - Google Patents

A kind of lead-acid accumulator light-type grid and preparation method thereof Download PDF

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CN107069042A
CN107069042A CN201710339644.7A CN201710339644A CN107069042A CN 107069042 A CN107069042 A CN 107069042A CN 201710339644 A CN201710339644 A CN 201710339644A CN 107069042 A CN107069042 A CN 107069042A
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lead
plating
grid
acid
aluminium alloy
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黄惠
周建峰
郭忠诚
陈步明
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KUNMING HENDERA SCIENCE AND TECHNOLOGY Co Ltd
Kunming University of Science and Technology
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KUNMING HENDERA SCIENCE AND TECHNOLOGY Co Ltd
Kunming University of Science and Technology
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C18/00Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
    • C23C18/16Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
    • C23C18/31Coating with metals
    • C23C18/32Coating with nickel, cobalt or mixtures thereof with phosphorus or boron
    • C23C18/34Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents
    • C23C18/36Coating with nickel, cobalt or mixtures thereof with phosphorus or boron using reducing agents using hypophosphites
    • CCHEMISTRY; METALLURGY
    • C23COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
    • C23CCOATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
    • C23C28/00Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D
    • C23C28/02Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D only coatings only including layers of metallic material
    • C23C28/023Coating for obtaining at least two superposed coatings either by methods not provided for in a single one of groups C23C2/00 - C23C26/00 or by combinations of methods provided for in subclasses C23C and C25C or C25D only coatings only including layers of metallic material only coatings of metal elements only
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/12Electroplating: Baths therefor from solutions of nickel or cobalt
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D3/00Electroplating: Baths therefor
    • C25D3/02Electroplating: Baths therefor from solutions
    • C25D3/34Electroplating: Baths therefor from solutions of lead
    • C25D3/36Electroplating: Baths therefor from solutions of lead characterised by the organic bath constituents used
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25DPROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
    • C25D5/00Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
    • C25D5/10Electroplating with more than one layer of the same or of different metals
    • C25D5/12Electroplating with more than one layer of the same or of different metals at least one layer being of nickel or chromium
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/661Metal or alloys, e.g. alloy coatings
    • H01M4/662Alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/665Composites
    • H01M4/667Composites in the form of layers, e.g. coatings
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/68Selection of materials for use in lead-acid accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/66Selection of materials
    • H01M4/68Selection of materials for use in lead-acid accumulators
    • H01M4/685Lead alloys
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/64Carriers or collectors
    • H01M4/70Carriers or collectors characterised by shape or form
    • H01M4/72Grids
    • H01M4/73Grids for lead-acid accumulators, e.g. frame plates
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

A kind of lead-acid accumulator light-type grid and preparation method thereof, including aluminium alloy grid (1), using plating or chemical plating method be plated in the nickel coating (2) of aluminium alloy grid surface, the plating lead layer (3) of nickel plating layer surface is plated in using electro-plating method.Compared with traditional metal grid, the addition of substrate aluminium can greatly improve grid performance in the present invention, and can reduce the consumption of lead, thus mitigate the weight of battery.Nickel coating is firmly combined with aluminium alloy plate grid base bottom, is formed the protective layer of structural integrity, can be greatly improved the specific energy and discharge capacity of battery.The light-type grid preparation section of the present invention is simple, and preparation cost is low, durable in use, can be used as the pole plate of Large Copacity, high-power output and long circulation life.

Description

A kind of lead-acid accumulator light-type grid and preparation method thereof
Technical field
The present invention relates to Lead-acid Battery Technology field, and in particular to lead-acid accumulator grid.
Technical background
Effect of the grid in battery has three aspects:One is to play skeletal support and viscous as the carrier of active material The effect of attached active material;Two be to play a part of afflux as the conductor of electric current, conflux and defeated stream;Three be as pole plate Equal fluid plays a part of making balanced current distribution into active material.
The alloy of the making grid used at present in production has three classes:One class is traditional lead-antimony alloy, and the content of antimony exists 4%~7% mass fraction;One class is low antimony or superlow antimony alloy, and the content of antimony is in 2% mass fraction or less than 1% mass Fraction;One class is lead calcium series, and actual is lead-calcium-tin-aluminium quaternary alloy, and the content of calcium is in 0.06%~0.1% mass point Number.The anode plate grid that above-mentioned alloy is cast, can all be oxidized to lead sulfate and brown lead oxide, finally in battery charging process Cause to lose the effect of support active material and make battery failure;Or due to the formation of brown lead oxide corrosion layer, make metal Stress is produced, makes the long large deformation of grid, this pole plate to be made integrally to be destroyed when deforming more than 4%, active material and grid Loose contact and come off, or at bus-bar it is short-circuit.
Lead-acid accumulator undergoes the development of more than 100 years, although its technology achieves very big breakthrough in all fields, but also There are many deficiencies, volume is big, weight is heavy, active material utilization is low, specific energy low (30-40Wh/kg) is that it is most prominent The deficiency and shortcoming gone out.From the point of view of the composition structure of lead-acid accumulator, the positive and negative grid of traditional lead acid batteries is main by density Larger metal is constituted, add the lead in the weight of lead-acid battery itself, grid quite a few only act as support and The effect confluxed, and it is not involved in the effect of battery itself discharge and recharge, therefore the specific energy of influence lead-acid battery.
Aluminium and its alloy are cheap, and density is low, but intensity is high, and plasticity is good, can be processed into various section bars, possess good Electric conductivity, thermal conductivity and corrosion resistance, the properties of battery can be effectively lifted as lead-acid battery grid material.But metal Aluminium is the metal of a kind of very living group, and the alundum (Al2O3) that surface is formed is a kind of amphoteric oxide, in sulfuric acid solution intolerant to Corruption candle.Therefore, metallic aluminium as the key of grid matrix be can its surface cover one layer with substrate be firmly combined with, structure Complete protective layer blocks the corrosion of electrolyte.
In recent years, it is many with the research of aluminium base light-type grid for lead-acid accumulator, such as Chinese patent 201310730624.4 prepare aluminium alloy grid and after its electroplate using gravity casting method, the side prepared with terne metal Frame carries out embedded cooperation and is used as grid material.Chinese patent 201010524211.7 with titanium or titanium alloy or copper or copper alloy or Aluminum or aluminum alloy powder or sheet material are substrate, and the powder that substrate is added into two or more predetermined substance is obtained through roll forming Obtain light plate grid for lead-acid storage battery.Chinese patent 201120070374.2, which is used, the countless cellular holes with carbon fibre material Cave aluminium foil honeycomb grid, lead plaster is filled up in hole, is used as polar plate of lead acid storage battery.Chinese patent 201310467238.0 is used Grid is made in carbon, aluminium or electrical conductivity alloy, and lead or metal are sprayed on after grid surface into strongly extruding or directly strong with rolled lead Power extrusion cladding prepares light-type grid in grid surface.Chinese patent 201110310109.1 is using porous aluminum or aluminum alloy Matrix, after pretreatment using fused salt chemistry lead plating and metal bath PROCESS FOR TREATMENT, obtains lead-acid battery with high specific surface area porous Aluminium base light plate grid etc..But these patented technologies all exist in terms of operation ease, preparation cost and aluminium lead binding ability It is not enough.
The content of the invention
In order to overcome the above-mentioned deficiencies of the prior art, the present invention provides a kind of plating lead layer adhesion in aluminum alloy substrate By force, lead-acid accumulator light-type grid that grid is lightweight, specific energy is higher and preparation method thereof.
The purpose of the present invention is achieved through the following technical solutions:
A kind of lead-acid accumulator light-type grid and preparation method thereof, including aluminium alloy grid, using plating or chemical plating Method is plated in the nickel coating of aluminium alloy grid surface, the plating lead layer of nickel plating layer surface is plated in using electro-plating method.
Aluminium alloy grid of the present invention is netted grid or radial grid or grid-like grid.It is described to use plating side The technical parameter that nickel coating is plated in aluminium alloy grid surface is by method:Electronickelling liquid composition is NiSO4·6H250~70g/L of O, 80~110g/L of trisodium citrate, H3BO35~8g/L, 8~10g/L of NaCl, Na2SO435~45g/L, 0.3~0.5g/ of gelatin L, using aluminium alloy grid as negative electrode, the close nickel plate of unilateral area be anode, 30~45 DEG C of plating temperature, current density 1~ 3Adm-2, electroplating time 30min~50min.Nickel coating is plated in the technology of aluminium alloy grid surface by the use chemical plating method Parameter is:Chemical nickel-plating liquid composition is NiSO4·6H2O20~50g/L, 20~35g/L of sodium hypophosphite, 15~30ml/ of lactic acid L, 1~3g/L of succinic acid, 1~3g/L of trisodium citrate, brightener 1ml/L, stabilizer 0.5g/L, add ammoniacal liquor regulation pH value and arrive 4.4~4.6,85 DEG C~90 DEG C of plating temperature, electroless plating time 1h~2h.The brightener composition is 1,4- butynediols 450 ~510g/L, 130~160g/L of epoxychloropropane, 3~5g/L of para toluene sulfonamide, 30~40g/L of sodium hydroxide;Stabilizer is Sodium Thiosulfate or thiocarbamide or lead chloride.The terne metal that the lead plating composition of layer is pure lead or Theil indices are 0~5%;Lead plating Layer is obtained using pyrovinic acid system or fluoboric acid system electro-plating method;The pyrovinic acid system electroplating technology parameter is:Electricity Lead plating liquid composition is 80~120ml/L of pyrovinic acid, 150~200g/L of pyrovinic acid lead, 0~50g/L Sn2+, sodium potassium tartrate tetrahydrate 2~5g/L, 0.5~5g/L of additive, pH=1~1.5,40 DEG C of plating temperature, current density 3Adm-2, 3~7h of electroplating time; The fluoboric acid system electroplating technology parameter is:Lead plating liquid composition be 190~220ml/L of fluoboric acid, 15~20g/L of boric acid, 180~220g/L of lead acetate, 0~30g/L of stannous fluoboric acid, gelatin 1g/L, thiocarbamide 0.2g/L, 40 DEG C of plating temperature, electric current is close Spend 3Adm-2, 4~7h of electroplating time.The additive is polyethylene glycol or hydroquinones.The thickness of the aluminium alloy grid is 1mm~2mm, nickel plating layer thick is 10 μm~50 μm, and lead plating thickness degree is 0.1mm~0.5mm.
The aluminium base light-type grid material of the present invention can be used for making accumulator plus-minus polar plate, with traditional metal grid phase Than the addition of substrate aluminium can greatly improve grid performance in the present invention, and can reduce the consumption of lead, thus mitigate battery Weight.Nickel coating is firmly combined with aluminium alloy plate grid base bottom, is formed the protective layer of structural integrity, can be greatly improved the matter of battery Measure specific energy and discharge capacity.The light-type grid preparation section of the present invention is simple, and preparation cost is low, durable in use, can be used as big The pole plate of capacity, high-power output and long circulation life.
Brief description of the drawings
Fig. 1 is the profile of lead-acid accumulator light-type grid of the present invention.
Embodiment
As shown in figure 1, the lead-acid accumulator of present invention light-type grid includes aluminium alloy grid 1, using plating or chemistry Electroplating method is plated in the nickel coating 2 of aluminium alloy grid surface, the plating lead layer 3 of nickel plating layer surface is plated in using electro-plating method.
Embodiment one:Reticulated aluminum alloy grid is placed in electronickelling liquid and electroplated, electronickelling liquid composition is NiSO4· 6H2O70g/L, trisodium citrate 90g/L, H3BO35g/L、NaCl 10g/L、Na2SO440g/L, gelatin 0.45g/L, with aluminium alloy Grid is negative electrode, and the close nickel plate of unilateral area is anode, 40 DEG C of plating temperature, current density 2Adm-2, electroplating time 30min, Nickel plating cleans drying after finishing with clear water, the grid after nickel plating is placed in into pyrovinic acid system lead plating again, lead plating liquid composition is Pyrovinic acid 120ml/L, pyrovinic acid lead 200g/L, sodium potassium tartrate tetrahydrate 2g/L, polyethylene glycol 0.5g/L, pH=1~1.2 are applied 40 DEG C of temperature is plated, by current density 3Adm-27h is electroplated, the lead-acid accumulator light-type grid that surface is pure lead-coat is obtained.Aluminium The thickness of alloy grid is 1mm, and nickel plating layer thick is 10 μm, and pure lead-coat thickness is 0.1mm.
Embodiment two:Radial aluminium alloy grid is placed in electronickelling liquid and electroplates 50min, electronickelling liquid composition is NiSO4·6H2O60g/L, trisodium citrate 110g/L, H3BO37g/L、NaCl 8g/L、Na2SO445g/L, gelatin 0.5g/L, with Aluminium alloy grid is negative electrode, and the close nickel plate of unilateral area is anode, 45 DEG C of plating temperature, current density 1Adm-2, electroplating time 40min, nickel plating cleans drying after finishing with clear water.Grid after nickel plating is placed in the plating lead plating of pyrovinic acid system, plating again Lead liquid composition is pyrovinic acid 90ml/L, pyrovinic acid lead 150g/L, 20g/L Sn2+, sodium potassium tartrate tetrahydrate 4g/L, hydroquinones 1.5g/L, pH=1~1.5,40 DEG C of plating temperature, by current density 3Adm-25h is electroplated, it is stanniferous to obtain surface plating lead layer The lead-acid accumulator light-type grid of 1.73% terne metal.The thickness of aluminium alloy grid is 2mm, and nickel plating layer thick is 30 μ M, pb-sn alloy plating thickness is 0.3mm.
Embodiment three:Grid-like aluminium alloy grid is placed in electronickelling liquid and electroplates 40min, electronickelling liquid composition is NiSO4·6H2O50g/L, trisodium citrate 80g/L, H3BO38g/L、NaCl 9g/L、Na2SO435g/L, gelatin 0.3g/L, with Aluminium alloy grid is negative electrode, and the close nickel plate of unilateral area is anode, 30 DEG C of plating temperature, current density 3Adm-2, electroplating time 50min, nickel plating cleans drying after finishing with clear water..Grid after nickel plating is placed in the plating lead plating of pyrovinic acid system, plating again Lead liquid composition is pyrovinic acid 80ml/L, pyrovinic acid lead 180g/L, 50g/L Sn2+, sodium potassium tartrate tetrahydrate 5g/L, polyethylene glycol 5g/L, pH=1.2~1.5,40 DEG C of plating temperature, by current density 3Adm-23h is electroplated, it is stanniferous 5% to obtain surface plating lead layer Terne metal lead-acid accumulator light-type grid.The thickness of aluminium alloy grid is 1.5mm, and nickel plating layer thick is 20 μm, lead Tin alloy coat thickness is 0.5mm.
Example IV:Grid-like aluminium alloy grid is placed in chemical nickel-plating liquid, chemical plating 1 hour when temperature is 90 DEG C, Chemical nickel-plating liquid composition is NiSO4·6H2O30g/L, sodium hypophosphite 30g/L, lactic acid 24ml/L, succinic acid 2g/L, citric acid (brightener composition is Isosorbide-5-Nitrae-butynediols 480g/L, epoxychloropropane 130g/L, to toluene sulphur by trisodium 1g/L, brightener 1ml/L Acid amides 5g/L, sodium hydroxide 40g/L), Sodium Thiosulfate 0.5g/L, add ammoniacal liquor and adjust pH value to 4.4~4.6.Chemical plating is complete Cheng Houyong clear water is dried after cleaning.Grid after nickel plating is placed in the plating lead plating of pyrovinic acid system again, lead plating method is with implementing Example two is identical, obtains the lead-acid accumulator light-type grid that overlay coating is terne metal.The thickness of aluminium alloy grid is 1.5mm, nickel plating layer thick is 25 μm, and pb-sn alloy plating thickness is 0.4mm.
Embodiment five:Radial aluminium alloy grid is placed in chemical nickel-plating liquid, chemical plating 2 hours when temperature is 85 DEG C, Chemical nickel-plating liquid composition is NiSO4·6H2O50g/L, sodium hypophosphite 20g/L, lactic acid 30ml/L, succinic acid 3g/L, citric acid (brightener composition is Isosorbide-5-Nitrae-butynediols 510g/L, epoxychloropropane 150g/L, to toluene sulphur by trisodium 3g/L, brightener 1ml/L Acid amides 3g/L, sodium hydroxide 30g/L), thiocarbamide 0.5g/L, add ammoniacal liquor and adjust pH value to 4.4~4.6.Used after the completion of chemical plating Clear water is dried after cleaning.Grid after nickel plating is placed in the plating lead plating of fluoboric acid system, lead plating liquid composition is fluoboric acid 220ml/L, boric acid 20g/L, lead acetate 180g/L, stannous fluoboric acid 20g/L, gelatin 1g/L, thiocarbamide 0.2g/L, plating temperature 40 DEG C, by current density 3Adm-26h is electroplated, the lead acid storage battery that overlay coating plates lead layer for the terne metal of stanniferous amount 2.07% is obtained Pond light-type grid.The thickness of aluminium alloy grid is 2mm, and nickel plating layer thick is 40 μm, and pb-sn alloy plating thickness is 0.4mm.
Embodiment six:Grid-like aluminium alloy grid is placed in chemical nickel-plating liquid, chemical plating 1.5 is small when temperature is 88 DEG C When, chemical nickel-plating liquid composition be the same as Example four.Grid after nickel plating is placed in the plating lead plating of fluoboric acid system, lead plating liquid composition For fluoboric acid 190ml/L, boric acid 18g/L, lead acetate 200g/L, stannous fluoboric acid 30g/L, gelatin 1g/L, thiocarbamide 0.2g/L is applied 40 DEG C of temperature is plated, by current density 3Adm-24h is electroplated, it is the terne metal plating lead layer that stanniferous amount is 1.94% to obtain overlay coating Lead-acid accumulator light-type grid.The thickness of aluminium alloy grid is 1.5mm, and nickel plating layer thick is 30 μm, pb-sn alloy plating Thickness is 0.3mm.
Embodiment seven:Reticulated aluminum alloy grid is placed in chemical nickel-plating liquid, chemical plating 1.5 hours when temperature is 90 DEG C, Chemical nickel-plating liquid composition is NiSO4·6H2O20g/L, sodium hypophosphite 35g/L, lactic acid 15ml/L, succinic acid 1g/L, citric acid (brightener composition is Isosorbide-5-Nitrae-butynediols 450g/L, epoxychloropropane 160g/L, to toluene sulphur by trisodium 2g/L, brightener 1ml/L Acid amides 4g/L, sodium hydroxide 35g/L), lead chloride 0.5g/L, add ammoniacal liquor and adjust pH value to 4.4~4.6.After the completion of chemical plating Dried after being cleaned with clear water.Grid after nickel plating is placed in the plating lead plating of fluoboric acid system, lead plating liquid composition is fluoboric acid 200ml/L, boric acid 15g/L, lead acetate 220g/L, gelatin 1g/L, thiocarbamide 0.2g/L, 40 DEG C of plating temperature, by current density 3Adm-27h is electroplated, the lead-acid accumulator light-type grid that overlay coating is pure lead is obtained.The thickness of aluminium alloy grid is 1.5mm, Nickel plating layer thick is 40 μm, and lead plating thickness degree is 0.4mm.

Claims (8)

1. a kind of lead-acid accumulator light-type grid and preparation method thereof, it is characterized in that, including aluminium alloy grid (1), using electricity Plating or chemical plating method are plated in the nickel coating (2) of aluminium alloy grid surface, the lead plating of nickel plating layer surface are plated in using electro-plating method Layer (3).
2. a kind of lead-acid accumulator light-type grid according to claim 1 and preparation method thereof, it is characterized in that, the aluminium Alloy grid is netted grid or radial grid or grid-like grid.
3. a kind of lead-acid accumulator light-type grid according to claim 1 and preparation method thereof, it is characterized in that, it is described to adopt It is by the technical parameter that nickel coating (2) is plated in aluminium alloy grid (1) surface with electro-plating method:Electronickelling liquid composition is NiSO4· 6H2O50~70g/L, 80~110g/L of trisodium citrate, H3BO35~8g/L, 8~10g/L of NaCl, Na2SO435~45g/L, 0.3~0.5g/L of gelatin, using aluminium alloy grid as negative electrode, the close nickel plate of unilateral area be anode, 30~45 DEG C of plating temperature, 1~3Adm of current density-2, electroplating time 30min~50min.
4. a kind of lead-acid accumulator light-type grid according to claim 1 and preparation method thereof, it is characterized in that, it is described to adopt It is by the technical parameter that nickel coating (2) is plated in aluminium alloy grid (1) surface with chemical plating method:Chemical nickel-plating liquid composition is NiSO4·6H2O20~50g/L, 20~35g/L of sodium hypophosphite, 15~30ml/L of lactic acid, 1~3g/L of succinic acid, citric acid three 1~3g/L of sodium, brightener 1ml/L, stabilizer 0.5g/L, addition ammoniacal liquor regulation pH value to 4.4~4.6,85 DEG C of plating temperature~ 90 DEG C, electroless plating time 1h~2h.
5. a kind of lead-acid accumulator light-type grid according to claim 4 and preparation method thereof, it is characterized in that, the light Bright dose of composition be 450~510g/L of 1,4- butynediols, 130~160g/L of epoxychloropropane, 3~5g/L of para toluene sulfonamide, 30~40g/L of sodium hydroxide;Stabilizer is Sodium Thiosulfate or thiocarbamide or lead chloride.
6. a kind of lead-acid accumulator light-type grid according to claim 1 and preparation method thereof, it is characterized in that, the plating The terne metal that lead layer composition is pure lead or Theil indices are 0~5%;Lead layer is plated using pyrovinic acid system or fluoboric acid system electricity Electroplating method is obtained;The pyrovinic acid system electroplating technology parameter is:Lead plating liquid composition be 80~120ml/L of pyrovinic acid, 150~200g/L of pyrovinic acid lead, 0~50g/L Sn2+, 2~5g/L of sodium potassium tartrate tetrahydrate, 0.5~5g/L of additive, pH=1~ 1.5,40 DEG C of plating temperature, current density 3Adm-2, 3~7h of electroplating time;The fluoboric acid system electroplating technology parameter is:Electricity Lead plating liquid composition be 190~220ml/L of fluoboric acid, 15~20g/L of boric acid, 180~220g/L of lead acetate, stannous fluoboric acid 0~ 30g/L, gelatin 1g/L, thiocarbamide 0.2g/L, 40 DEG C of plating temperature, current density 3Adm-2, 4~7h of electroplating time.
7. a kind of lead-acid accumulator light-type grid according to claim 6 and preparation method thereof, it is characterized in that, it is described to add Plus agent is polyethylene glycol or hydroquinones.
8. a kind of lead-acid accumulator light-type grid according to any one of claim 1~7 and preparation method thereof, it is special Levying is, the thickness of the aluminium alloy grid is 1mm~2mm, and nickel plating layer thick is 10 μm~50 μm, and lead plating thickness degree is 0.1mm ~0.5mm.
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CN107665995A (en) * 2017-09-05 2018-02-06 超威电源有限公司 A kind of lead-acid battery aluminium base grid and preparation method thereof, preparation facilities
CN109841837A (en) * 2017-11-28 2019-06-04 中国科学院大连化学物理研究所 Lead carbon battery grid and preparation and application of the galvanoplastic preparation with three-dimensional structure
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CN110923769A (en) * 2019-10-21 2020-03-27 肇庆理士电源技术有限公司 Electroplating method of thin lead coating of carbon grid of lead-carbon battery
CN110923769B (en) * 2019-10-21 2021-04-20 肇庆理士电源技术有限公司 Electroplating method of thin lead coating of carbon grid of lead-carbon battery
CN112736366A (en) * 2020-12-29 2021-04-30 上海应用技术大学 Method for cast welding light metal negative grid lead storage battery busbar
CN116454524A (en) * 2023-05-31 2023-07-18 三一红象电池有限公司 Explosion-proof valve and preparation method and application thereof

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