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 PDFInfo
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- 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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- acid
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- accumulator plate
- acid accumulator
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K35/00—Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
- B23K35/22—Rods, electrodes, materials, or media, for use in soldering, welding, or cutting characterised by the composition or nature of the material
- B23K35/36—Selection 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
- B23K35/3612—Selection 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
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B23—MACHINE TOOLS; METAL-WORKING NOT OTHERWISE PROVIDED FOR
- B23K—SOLDERING OR UNSOLDERING; WELDING; CLADDING OR PLATING BY SOLDERING OR WELDING; CUTTING BY APPLYING HEAT LOCALLY, e.g. FLAME CUTTING; WORKING BY LASER BEAM
- B23K35/00—Rods, electrodes, materials, or media, for use in soldering, welding, or cutting
- B23K35/40—Making wire or rods for soldering or welding
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- 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
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)
- 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. 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. 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. 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. 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. 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.
- 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.
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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 |
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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 |
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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 |
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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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