CN105171272B - A kind of lead-acid accumulator plate flux and preparation method thereof - Google Patents

A kind of lead-acid accumulator plate flux and preparation method thereof Download PDF

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Publication number
CN105171272B
CN105171272B CN201510558852.7A CN201510558852A CN105171272B CN 105171272 B CN105171272 B CN 105171272B CN 201510558852 A CN201510558852 A CN 201510558852A CN 105171272 B CN105171272 B CN 105171272B
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Prior art keywords
acid
lead
accumulator plate
acid accumulator
solvent
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CN105171272A (en
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吴飞
孙震
王振
李文斌
丁刚强
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HUBEI GREATSEA NEWPOWER TECHNOLOGY Co Ltd
712th Research Institute of CSIC
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HUBEI GREATSEA NEWPOWER TECHNOLOGY Co Ltd
712th Research Institute of CSIC
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23KSOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
    • B23K35/00Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
    • B23K35/22Rods, electrodes, materials, or media, for use in soldering, welding, or cutting characterised by the composition or nature of the material
    • B23K35/36Selection of non-metallic compositions, e.g. coatings, fluxes; Selection of soldering or welding materials, conjoint with selection of non-metallic compositions, both selections being of interest
    • B23K35/3612Selection of non-metallic compositions, e.g. coatings, fluxes; Selection of soldering or welding materials, conjoint with selection of non-metallic compositions, both selections being of interest with organic compounds as principal constituents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B23MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
    • B23KSOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
    • B23K35/00Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
    • B23K35/40Making wire or rods for soldering or welding

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Battery Electrode And Active Subsutance (AREA)

Abstract

The present invention relates to a kind of lead-acid accumulator plate flux and preparation method thereof.The lead-acid accumulator plate flux, its each component and mass percent(wt%)For:Organic acid for activating agent 12% ~ 25%, surfactant 0.2% ~ 0.5%, mixed organic solvents 40% ~ 60%, deionized water 15% ~ 45%.The preparation method of the lead-acid accumulator plate flux, comprises the steps:First under normal temperature condition, solvent, deionized water and organic acid for activating agent are successively blended with proportion to add in stirred tank, and 30 ~ 60min is at the uniform velocity then stirred with 80 ~ 120rpm speed, then adds surfactant, 15 ~ 20min of stirring is further continued for, it is last filling.Cast welding agent provided by the invention and compound method are simple, without with do not produce extremely toxic substance, suitable for various pole plate alloys, and good with the compatibility of alloy, frost resistance is preferable, is advantageous to improve the qualification rate of pole plate welding.

Description

A kind of lead-acid accumulator plate flux and preparation method thereof
Technical field
The invention belongs to battery technology field, is related to a kind of scaling powder and preparation method thereof, more particularly to a kind of plumbic acid Accumulator plate scaling powder and preparation method thereof.
Background technology
Lead-acid accumulator is mainly by positive plate, negative plate, electrolyte, dividing plate, battery case, battery cover, pole, fill cap etc. Composition, has the advantages that cheap, service life is long, job stability is high, good reliability.Lead-acid accumulator it is practical with Come, be widely used in all conglomeraties such as electric power, traffic, communication, power station, emergency power supply as power supply.Recent decades, power supply skill Art develops rapidly, and novel storage battery is continuously developed out and moves towards market, but lead-acid accumulator still occupies in field of power supplies Very important status.
The manufacturing technology comparative maturity of lead-acid accumulator, mainly including gold conjugate-cast panel grid-smear-solidification, dry Dry-burst polishing-combo-pack piece-pole plate weld-fills shell-above lid sealing-terminal welds-and enters groove-acid filling-change Into-clean the links such as storage.The welding of accumulator plate and bus-bar uses automatic soldering technique mostly, welding quality it is good The bad performance and used life for directly affecting lead-acid accumulator.The selection of scaling powder determines that pole plate welds matter to a certain extent Amount, so as to cause to directly affect to the quality of whole lead-acid accumulator.
At present, the scaling powder that domestic and international battery manufacturing firm generally uses is divided into oiliness and water-based two class.Oiliness helps weldering Agent is prepared, such as generally using organic carboxyl acids such as ethanedioic acid, succinic acid as activator with polyethylene glycol, glycerine etc. for primary solvent Chinese patent [CN102728817A] is provided using 3 ~ 6wt% ethanedioic acid as activator, and weldering is helped as solvent using glycerine, propyl alcohol Agent, Chinese patent [CN103521948A] are provided using 5 ~ 10wt% dimethylolpropionic acid as activator, using ethanol, propyl alcohol as The scaling powder of solvent.Such scaling powder is pretty good to lead-antimony alloy pole plate welding effect, but to lead-calcium alloy pole plate welding effect compared with Difference, and its winter easily solidifies, reactivity is weaker, it is difficult to cause cast welded mold to be cleared up, solder yield is low.It is existing water-based to help weldering Agent is prepared, such as Chinese patent mostly with sulfuric acid, phosphorous acid, metaphosphoric acid etc. for activator by solvent of deionized water [CN103264239A] provides the scaling powder using 10 ~ 15wt% sulfuric acid as activator, and Chinese patent [CN104475712A] carries The scaling powder using 3 ~ 5wt% phosphorous acid as activator is supplied, Chinese patent [CN103706966A] is provided with 8 ~ 15wt%'s Metaphosphoric acid is the scaling powder of activator.This kind of water-based scaling powder anti-flammability is preferable but poor with the compatibility of lug, is also easy to produce void Phenomena such as weldering, dry joint.In addition, the corrosivity such as sulfuric acid as activator is too strong and is easily retained on lug, cause the table of lug Face forms oxide layer.Effective Storage period of phosphorous acid and metaphosphoric acid is shorter, and phosphorous acid is heated produces severe toxicity in use Hydrogen phosphide, and the chemicals that metaphosphoric acid is inherently hypertoxic is good for using such scaling powder to operating environment and operating personnel Kang Zaocheng significant damages.
The content of the invention
Present invention is generally directed to the weak point of existing scaling powder, there is provided a kind of lead-acid accumulator plate flux and its system Preparation Method.The scaling powder has the features such as applicability is wide, good with the compatibility of alloy, and solder yield is high and the feature of environmental protection is good.Together When, the present invention also provides the preparation method of the scaling powder.
The purpose of the present invention is realized by following technological approaches:
A kind of lead-acid accumulator plate flux, its each component and mass percent(wt%)For:Organic acid for activating agent 12% ~ 25%, surfactant 0.2% ~ 0.5%, mixed organic solvents 40% ~ 60%, deionized water 15% ~ 45%.
Further technical scheme is:
Described lead-acid accumulator plate flux, its each component and mass percent are:Organic acid for activating agent 20%, table Face activating agent 0.2%, mixed organic solvents 50%, deionized water 29.8%.
Described lead-acid accumulator plate flux, its each component and mass percent are:Organic acid for activating agent 12%, table Face activating agent 0.5%, mixed organic solvents 45%, deionized water 42.5%.
Described lead-acid accumulator plate flux, the organic acid for activating agent is selected from benzene sulfonic acid, p-methyl benzenesulfonic acid, right Hydroxy benzene sulfonic acid, for one kind in three, or 2 kinds therein, or 3 kinds of combination.
Described lead-acid accumulator plate flux, the surfactant are:TX-10, or/and TX-10 phosphates.
Described lead-acid accumulator plate flux, the mixed organic solvents are mixed by high boiling solvent and low boiling point solvent Conjunction forms, and wherein high boiling solvent is in three selected from 1-METHYLPYRROLIDONE, ethylene glycol monobutyl ether, dimethylformamide One kind, or 2 kinds therein, or 3 kinds of combination;Low boiling point solvent is methanol, or/and isopropanol.
Described lead-acid accumulator plate flux, the matter of high boiling solvent and low boiling point solvent in its mixed organic solvents Amount is than being 1~1.5:1.
Described lead-acid accumulator plate flux, the matter of high boiling solvent and low boiling point solvent in its mixed organic solvents Amount is than being 1:1.
Described lead-acid accumulator plate flux, the matter of high boiling solvent and low boiling point solvent in its mixed organic solvents Amount is than being 1.3:1.
A kind of preparation method of lead-acid accumulator plate flux of the present invention, comprises the steps:
First under normal temperature condition, solvent, deionized water and organic acid for activating agent are successively blended with proportion and is added Enter in stirred tank, 30 ~ 60min is at the uniform velocity then stirred with 80 ~ 120rpm speed, then adds surfactant, be further continued for stirring 15 ~ 20min is mixed, it is last filling.
Beneficial effects of the present invention:
Cast welding agent composition provided by the invention and compound method are simple, suitable for various pole plate alloys, and with the phase of alloy Capacitive is good, and frost resistance is good, is advantageous to improve the qualification rate of pole plate welding.In addition, the scaling powder is free of and does not produce extremely toxic substance, Cast welding operating environment is greatly improved, avoids body harm of the cast welding technical process to operating personnel.
Embodiment
It is as follows that the invention will be further described in conjunction with the embodiments:
Embodiment 1:It is lead-acid accumulator plate flux basic embodiment of the present invention.A kind of polar plate of lead acid storage battery helps weldering Agent, its each component and mass percent are:Organic acid for activating agent 12% ~ 25%, surfactant 0.2% ~ 0.5%, mixing are organic molten Agent 40% ~ 60%, deionized water 15% ~ 45%.
The preparation method of the lead-acid accumulator plate flux, step are:First under normal temperature condition, in proportion successively Solvent, deionized water and organic acid for activating agent is blended with to add in stirred tank, it is then even with 80 ~ 120rpm speed Speed 30 ~ 60min of stirring, then adds surfactant, is further continued for 15 ~ 20min of stirring, last filling.
Embodiment 2:It is further embodiment.Described lead-acid accumulator plate flux, its organic acid for activating agent Selected from benzene sulfonic acid, p-methyl benzenesulfonic acid, p-hydroxybenzenyl sulfonate, for one kind in three, or 2 kinds therein, or 3 kinds of combination. The surfactant is:TX-10, or/and TX-10 phosphates.The mixed organic solvents are by high boiling solvent and low boiling Solvent mixes, and wherein high boiling solvent is selected from 1-METHYLPYRROLIDONE, ethylene glycol monobutyl ether, dimethylformamide One kind in three, or 2 kinds therein, or 3 kinds of combination;Low boiling point solvent is methanol, or/and isopropanol.Described mixing The mass ratio of high boiling solvent and low boiling point solvent is 1~1.5 in organic solvent:1.
Embodiment 3:It is further embodiment.Described lead-acid accumulator plate flux, its each component and quality hundred Fraction is:Organic acid for activating agent 20%, surfactant 0.2%, mixed organic solvents 50%, deionized water 29.8%;It is mixed The mass ratio of high boiling solvent and low boiling point solvent is 1 in organic solvent:1.
Embodiment 4:It is further embodiment.Described lead-acid accumulator plate flux, its each component and quality hundred Fraction is:Organic acid for activating agent 12%, surfactant 0.5%, mixed organic solvents 45%, deionized water 42.5%;It is mixed with The mass ratio of high boiling solvent and low boiling point solvent is 1.3 in solvent:1.
It is further preferred embodiment below:
Embodiment 4:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent wt%:
Benzene sulfonic acid:20wt%
TX-10:0.2wt%
1-METHYLPYRROLIDONE:30wt%
Methanol:20wt%
Deionized water:29.8wt%
Preparation method:Under normal temperature condition, by the mixed liquor of load weighted 1-METHYLPYRROLIDONE and methanol, deionization Water, benzene sulfonic acid are sequentially added in stirred tank, are at the uniform velocity stirred 60min with 80rpm speed, are then added TX-10, are continued Stirring 20min can be filling.
Embodiment 5:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent:
P-methyl benzenesulfonic acid:12wt%
TX-10:0.5wt%
Ethylene glycol monobutyl ether:25wt%
Isopropanol:20wt%
Deionized water:42.5wt%
Preparation method:Under normal temperature condition, by the mixed liquor of load weighted ethylene glycol monobutyl ether and isopropanol, deionization Water, p-methyl benzenesulfonic acid are sequentially added in stirred tank, are at the uniform velocity stirred 45min with 100rpm speed, are then added TX- 10, continuing stirring 18min can be filling.
Embodiment 6:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent:
P-hydroxybenzenyl sulfonate:25wt%
TX-10 phosphates:0.4wt%
Ethylene glycol monobutyl ether:20wt%
Methanol:20wt%
Deionized water:34.6wt%
Preparation method:Under normal temperature condition, by the mixed liquor of load weighted ethylene glycol monobutyl ether and methanol, deionized water, P-hydroxybenzenyl sulfonate is sequentially added in stirred tank, is at the uniform velocity stirred 40min with 120rpm speed, is then added TX-10 Phosphate, continuing stirring 15min can be filling.
Embodiment 7:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent:
Benzene sulfonic acid:8wt%
P-methyl benzenesulfonic acid:10wt%
TX-10 phosphates:0.3wt%
1-METHYLPYRROLIDONE:15wt%
Ethylene glycol monobutyl ether:10wt%
Isopropanol:25wt%
Deionized water:31.7wt%
Preparation method:Under normal temperature condition, by load weighted 1-METHYLPYRROLIDONE, ethylene glycol monobutyl ether and isopropanol Mixed liquor, deionized water, benzene sulfonic acid, p-methyl benzenesulfonic acid are sequentially added in stirred tank, are at the uniform velocity stirred with 100rpm speed 40min is mixed, then adds TX-10 phosphates, continuing stirring 20min can be filling.
Embodiment 8:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent:
Benzene sulfonic acid:10wt%
P-methyl benzenesulfonic acid:10wt%
TX-10:0.3wt%
TX-10 phosphates:0.1wt%
1-METHYLPYRROLIDONE:15wt%
Ethylene glycol monobutyl ether:10wt%
Isopropanol:15wt%
Methanol:10wt%
Deionized water:29.6wt%
Preparation method:Under normal temperature condition, by load weighted 1-METHYLPYRROLIDONE, ethylene glycol monobutyl ether, isopropanol and Mixed liquor, deionized water, benzene sulfonic acid, the p-methyl benzenesulfonic acid of methanol are sequentially added in stirred tank, with 100rpm speed 50min is at the uniform velocity stirred, then adds TX-10, TX-10 phosphate, continuing stirring 15min can be filling.
Embodiment 9:The raw material of described lead-acid accumulator plate flux is weighed by following mass percent:
Benzene sulfonic acid:15wt%
P-methyl benzenesulfonic acid:8wt%
TX-10:0.2wt%
TX-10 phosphates:0.2wt%
1-METHYLPYRROLIDONE:10wt%
Ethylene glycol monobutyl ether:15wt%
Methanol:20wt%
Deionized water:31.6wt%
Preparation method:Under normal temperature condition, by the mixed of load weighted 1-METHYLPYRROLIDONE, ethylene glycol monobutyl ether and methanol Close liquid, deionized water, benzene sulfonic acid, p-methyl benzenesulfonic acid sequentially to add in stirred tank, at the uniform velocity stirred with 120rpm speed 30min, TX-10, TX-10 phosphate are then added, continuing stirring 20min can be filling.
Protection scope of the present invention is not limited to above-described embodiment.

Claims (7)

  1. A kind of 1. lead-acid accumulator plate flux, it is characterised in that:Each component and mass percent are:Organic acid for activating agent 12% ~ 25%, surfactant 0.2% ~ 0.5%, mixed organic solvents 40% ~ 60%, deionized water 15% ~ 45%;The organic acid is lived Agent is selected from benzene sulfonic acid, p-methyl benzenesulfonic acid, p-hydroxybenzenyl sulfonate, for one kind in three, or 2 kinds therein, or 3 kinds of group Close;The mixed organic solvents are mixed by high boiling solvent and low boiling point solvent, and wherein high boiling solvent is selected from N- first Base pyrrolidones, ethylene glycol monobutyl ether, dimethylformamide, for one kind in three, or 2 kinds therein, or 3 kinds of combination; Low boiling point solvent is methanol, or/and isopropanol;The mass ratio of high boiling solvent and low boiling point solvent is 1 in mixed organic solvents ~1.5:1.
  2. 2. lead-acid accumulator plate flux according to claim 1, it is characterised in that:Each component and mass percent For:Organic acid for activating agent 20%, surfactant 0.2%, mixed organic solvents 50%, deionized water 29.8%.
  3. 3. lead-acid accumulator plate flux according to claim 1, it is characterised in that:Each component and mass percent For:Organic acid for activating agent 12%, surfactant 0.5%, mixed organic solvents 45%, deionized water 42.5%.
  4. 4. lead-acid accumulator plate flux according to claim 1, it is characterised in that:The surfactant is:TX- 10, or/and TX-10 phosphates.
  5. 5. lead-acid accumulator plate flux according to claim 1, in its mixed organic solvents high boiling solvent with it is low The mass ratio of boiling point solvent is 1:1.
  6. 6. lead-acid accumulator plate flux according to claim 1, in its mixed organic solvents high boiling solvent with it is low The mass ratio of boiling point solvent is 1.3:1.
  7. A kind of 7. preparation method of lead-acid accumulator plate flux described in claim 1, it is characterised in that:Including following steps Suddenly:
    First under normal temperature condition, solvent, deionized water and organic acid for activating agent addition are successively blended with proportion and is stirred Mix in kettle, 30 ~ 60min at the uniform velocity then stirred with 80 ~ 120rpm speed, then adds surfactant, be further continued for stirring 15 ~ 20min, it is last filling.
CN201510558852.7A 2015-09-06 2015-09-06 A kind of lead-acid accumulator plate flux and preparation method thereof Active CN105171272B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108637526A (en) * 2018-04-26 2018-10-12 天能集团(河南)能源科技有限公司 A kind of lead-acid accumulator high-performance scaling powder and preparation method thereof

Families Citing this family (4)

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CN110549036A (en) * 2018-06-03 2019-12-10 湖北鹏林新材料科技有限公司 Organic soldering flux and preparation method thereof
CN110076479B (en) * 2019-03-25 2021-04-27 武汉谊盛新材料科技有限公司 Neutral flux for cast welding of lead-acid storage battery plate group and preparation method thereof
CN112171110A (en) * 2020-09-17 2021-01-05 东莞市麦克莱恩新材料有限公司 Preparation method of novel water-based stainless steel soldering flux
CN112582688A (en) * 2020-11-16 2021-03-30 超威电源集团有限公司 Manufacturing device and method of lead-acid storage battery

Family Cites Families (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1233499C (en) * 2002-10-18 2005-12-28 深圳市唯特偶化工开发实业有限公司 Halogen-free low-solid-contained water-base washing-free scaling powder
CN101244493B (en) * 2008-03-21 2010-08-11 天津市瑞星高新技术发展公司 Aluminum alloy leadless welding wire containing soldering fluid and method for manufacturing soldering fluid
CN102248326A (en) * 2010-05-20 2011-11-23 骆驼集团股份有限公司 Organic aqueous flux for lead-acid storage battery pole group automatic welding and preparation method thereof
CN101890596A (en) * 2010-07-23 2010-11-24 深圳市亿铖达工业有限公司 Low-carbon environmentally-friendly water-based soldering flux
CN103273223B (en) * 2013-06-17 2015-04-15 北京朝铂航科技有限公司 Water-based soldering flux capable of reducing discharge of tin soldering pollutants
CN103521948B (en) * 2013-10-08 2015-10-21 无锡华燕新电源有限公司 Battery cast welded scaling powder of a kind of colloid power and preparation method thereof
CN104985355A (en) * 2015-07-01 2015-10-21 芜湖市爱德运输机械有限公司 Lead-free solder scaling powder and preparation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108637526A (en) * 2018-04-26 2018-10-12 天能集团(河南)能源科技有限公司 A kind of lead-acid accumulator high-performance scaling powder and preparation method thereof
CN108637526B (en) * 2018-04-26 2020-08-11 天能集团(河南)能源科技有限公司 High-performance soldering flux for lead-acid storage battery and preparation method thereof

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