CN106099049B - A kind of anode mixing paste technology - Google Patents
A kind of anode mixing paste technology Download PDFInfo
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- CN106099049B CN106099049B CN201610499741.8A CN201610499741A CN106099049B CN 106099049 B CN106099049 B CN 106099049B CN 201610499741 A CN201610499741 A CN 201610499741A CN 106099049 B CN106099049 B CN 106099049B
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
- H01M4/16—Processes of manufacture
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
- H01M4/16—Processes of manufacture
- H01M4/20—Processes of manufacture of pasted electrodes
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
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- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
A kind of anode mixing paste technology, is related to battery technology field, comprising the following steps: (1) do stirring: raw material is mixed and stirred for 5-7min;(2) wet stirring: being added pure water, continues to stir 4-5min;(3) acid adding: sulfuric acid is added, and continues to stir;(4) water cooling: when cream temperature is 55-58 DEG C, start circulating water cooling;(5) air-cooled: when cream temperature is between 65-75 DEG C, to start air cooling;(6) go out cream: the mixing time after acid adding is more than or equal to 7min, and paste outer temperature is less than or equal to 48 DEG C.The present invention provides a kind of positive mixing paste technologies, the battery manufactured using the technique, the content and ratio of the 3BS and 4BS in anode diachylon after the completion of solidification is suitable, without in addition adding 3BS and 4BS crystal seed, so that the lead-acid accumulator prepared has the advantages that long life, high battery performance and low production cost.
Description
Technical field
The present invention relates to battery technology field more particularly to a kind of positive mixing paste technologies.
Background technique
Electric vehicle is a kind of environment-friendly type walking-replacing tool in China at present, and electronic automobile-used lead storage battery is electric vehicle core
Part, dosage is very big, is a kind of battery that high rate cyclic uses, and design requirement is reasonable, and it is stringent to cross range request.In lead-acid accumulator
In production process, the quality of critical process of the mixing paste as battery process, quality directly affects the performance of battery.It is especially electric
The service life in pond and battery initial performance.And the initial performance and battery life of battery, and directly used with vast lead-acid accumulator
The demand of person is corresponding.The formula and manufacturing method of anode diachylon also determine the performance of lead storage battery to a certain extent.
Traditional positive mixing paste, temperature are controlled at 68 DEG C or so, and temperature determines in the anode diachylon after solidifying
3BS and 4BS content, wherein 4BS determines the service life of battery, and 3BS determines the performance of battery, using existing skill
The battery that the temperature provided in art is made still has biggish defect, in order to improve performance and the service life of battery, part factory
Family is added with the additives such as 4BS crystal seed in mixing paste in the feed, and although battery performance is improved to some extent, but defect
It still has, and increases manufacturing cost.
Summary of the invention
The present invention provides a kind of positive mixing paste technology, using the technique system to solve the disadvantage that the above-mentioned prior art
The battery made can have the advantages that long life, high battery performance and low production cost.
Invention is achieved in that a kind of positive mixing paste technology, comprising the following steps: (1) does stirring: being by parts by weight
1024.2-1051 raw material be mixed and stirred for 5-7min;(2) wet stirring: the pure water that parts by weight are 110-130 is added, continues to stir
Mix 4-5min;(3) acid adding: addition parts by weight are 88.8-89.2, density 1.4g/cm3The sulfuric acid of (25 DEG C), acid addition time are
11-13min, and continue to stir;(4) water cooling: when cream temperature is 55-58 DEG C, start circulating water cooling;(5) air-cooled: when cream temperature is
When between 65-75 DEG C, start air cooling;(6) go out cream: the mixing time after acid adding is more than or equal to 7min, and paste outer temperature is less than
Equal to 48 DEG C, paste density when cream is 4.4-4.5g/cm out3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 990-1010 parts of lead powder, additive 4.7-
5.0 parts, 1.4-2 parts of lead orthoplumbate, 20-24 parts of fecula, sour 8-10 parts of the powder of leaching.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Compared with the existing technology, the beneficial effects of the present invention are:
Compared with prior art, the present invention a kind of positive mixing paste technology is provided, the battery manufactured using the technique, Gu
The content and ratio of the 3BS and 4BS in anode diachylon after the completion of change is suitable, does not have in addition addition 3BS and 4BS crystal seed, so that
The lead-acid accumulator prepared has the advantages that long life, high battery performance and low production cost.
Detailed description of the invention
Fig. 1 is battery cycle life curve of the invention.
Specific embodiment
Embodiment 1
A kind of anode mixing paste technology, comprising the following steps: (1) do stirring: the raw material that parts by weight are 1024.2-1051 is mixed
Merge stirring 5-7min;(2) wet stirring: being added the pure water that parts by weight are 110-130, continues to stir 4-5min;(3) acid adding: add
Entering parts by weight is 88.8-89.2, density 1.4g/cm3Sulfuric acid, acid addition time 11-13min, and continue to stir;(4) water
It is cold: when cream temperature is 55-58 DEG C, to start circulating water cooling;(5) air-cooled: when cream temperature is between 65-75 DEG C, to start air cooling;
(6) go out cream: the mixing time after acid adding is more than or equal to 7min, and paste outer temperature is less than or equal to 48 DEG C, out paste density when cream
For 4.4-4.5g/cm3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 990-1010 parts of lead powder, additive 4.7-
5.0 parts, 1.4-2 parts of lead orthoplumbate, 20-24 parts of fecula, sour 8-10 parts of the powder of leaching.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Embodiment 2
A kind of anode mixing paste technology, comprising the following steps: (1) do stirring: the raw material that parts by weight are 1024.2 is mixed simultaneously
Stir 5min;(2) wet stirring: being added the pure water that parts by weight are 110, continues to stir 4min;(3) acid adding: parts by weight, which are added, is
88.8, density 1.4g/cm3Sulfuric acid, acid addition time 11min, and continue to stir;(4) water cooling: when cream temperature is 55 DEG C,
Start circulating water cooling;(5) air-cooled: when cream temperature is 65 DEG C, to start air cooling;(6) go out cream: the mixing time etc. after acid adding
In 7min, paste outer temperature is equal to 48 DEG C, and paste density when cream is 4.4g/cm out3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 990 parts of lead powder, 4.7 parts of additive, four
It aoxidizes 1.4 parts of three lead, 20 parts of fecula, drench sour 8 parts of powder.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Embodiment 3
A kind of anode mixing paste technology, comprising the following steps: (1) do stirring: the raw material that parts by weight are 1051 is mixed and is stirred
Mix 7min;(2) wet stirring: being added the pure water that parts by weight are 130, continues to stir 5min;(3) acid adding: it is 89.2 that parts by weight, which are added,
Density is 1.4g/cm3Sulfuric acid, acid addition time 13min, and continue to stir;(4) water cooling: when cream temperature is 58 DEG C, starting is followed
The cooling of ring water;(5) air-cooled: when cream temperature is 75 DEG C, to start air cooling;(6) go out cream: the mixing time after acid adding is equal to
9min, paste outer temperature are equal to 45 DEG C, and paste density when cream is 4.5g/cm out3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 1010 parts of lead powder, 5.0 parts of additive, four
It aoxidizes 2 parts of three lead, 24 parts of fecula, drench sour 10 parts of powder.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Embodiment 4
A kind of anode mixing paste technology, comprising the following steps: (1) do stirring: the raw material that parts by weight are 1037.5 is mixed simultaneously
Stir 6min;(2) wet stirring: being added the pure water that parts by weight are 120, continues to stir 4.5min;(3) acid adding: parts by weight, which are added, is
89, density 1.4g/cm3Sulfuric acid, acid addition time 12min, and continue to stir;(4) it water cooling: when cream temperature is 57 DEG C, opens
Dynamic circulating water cooling;(5) air-cooled: when cream temperature is 73 DEG C, to start air cooling;(6) go out cream: the mixing time after acid adding is equal to
10min, paste outer temperature are equal to 45 DEG C, and paste density when cream is 4.4g/cm out3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 1000 parts of lead powder, 4.8 parts of additive, four
It aoxidizes 1.7 parts of three lead, 22 parts of fecula, drench sour 9 parts of powder.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Other embodiments
A kind of anode mixing paste technology, comprising the following steps:
Table 1
It is implemented the steps of according to embodiment any combination of each variable in table 1:
(1) it does stirring: the raw material that parts by weight are 1024.2-1051 is mixed and stirred for 5-7min;(2) it wet stirring: is added
Parts by weight are the pure water of 110-130, continue to stir 4-5min;(3) acid adding: addition parts by weight are 88.8-89.2, and density is
1.4g/cm3Sulfuric acid, acid addition time 11-13min, and continue to stir;(4) water cooling: when cream temperature is 55-58 DEG C, starting is followed
The cooling of ring water;(5) air-cooled: when cream temperature is between 65-75 DEG C, to start air cooling;(6) go out cream: the mixing time after acid adding
More than or equal to 7min, paste outer temperature is less than or equal to 48 DEG C, and paste density when cream is 4.4-4.5g/cm out3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 990-1010 parts of lead powder, additive 4.7-
5.0 parts, 1.4-2 parts of lead orthoplumbate, 20-24 parts of fecula, sour 8-10 parts of the powder of leaching.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Experimental example
The positive mixing paste technology of contrast groups, comprising the following steps: (1) do stirring: being 1000 parts of lead powder, addition by parts by weight
4.8 parts of agent, 1.7 parts of lead orthoplumbate, 22 parts of fecula, sour 9 parts of the powder of leaching are mixed and stirred for 6min;(2) parts by weight wet stirring: are added
For 120 pure water, continue to stir 4.5min;(3) acid adding: it is 89 that parts by weight, which are added, density 1.4g/cm3Sulfuric acid, when acid adding
Between be 12min, and continue to stir;(4) water cooling: when cream temperature is 57 DEG C, start circulating water cooling;(5) air-cooled: when cream temperature is 68
DEG C when, start air cooling;(6) go out cream: the mixing time after acid adding is equal to 10min, and paste outer temperature is equal to 40 DEG C, out when cream
Paste density is 4.4g/cm3.Wherein, fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.Leaching
Sour powder is made of the lead sulfate of 40%-60%, remaining ingredient is lead.Additive is staple fiber, antimony oxide, stannous sulfate and receives
Meter Shi Mo.
The positive mixing paste technology of experimental group, comprising the following steps: (1) do stirring: the raw material that parts by weight are 1037.5 is mixed
Merge stirring 6min;(2) wet stirring: being added the pure water that parts by weight are 120, continues to stir 4.5min;(3) weight acid adding: is added
Part is 89, density 1.4g/cm3Sulfuric acid, acid addition time 12min, and continue to stir;(4) water cooling: when cream temperature is 57 DEG C
When, start circulating water cooling;(5) air-cooled: when cream temperature is 73 DEG C, to start air cooling;(6) go out cream: when stirring after acid adding
Between be equal to 10min, paste outer temperature be equal to 45 DEG C, out paste density when cream be 4.4g/cm3。
Raw material in the step (1) is grouped as by the group of following parts by weight: 1000 parts of lead powder, 4.8 parts of additive, four
It aoxidizes 1.7 parts of three lead, 22 parts of fecula, drench sour 9 parts of powder.
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up.
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
The additive is staple fiber, antimony oxide, stannous sulfate and nano-graphite.
Table 2
It can be seen that from table 2 and Fig. 1, relative to contrast groups, the 4BS content of experimental group is promoted to by original 3% or so
10% or so, battery life is improved by original 350 times or so to 450 or so.
Embodiment described above, only one kind of the present invention more preferably specific embodiment, those skilled in the art
The usual variations and alternatives that member carries out within the scope of technical solution of the present invention are intended to be included in protection scope of the present invention.
Claims (2)
1. a kind of anode mixing paste technology, it is characterised in that: the following steps are included: (1) dry stirring: being 1024.2- by parts by weight
1051 raw material is mixed and stirred for 5-7min;(2) wet stirring: being added the pure water that parts by weight are 110-130, continues to stir 4-
5min;(3) acid adding: addition parts by weight are 88.8-89.2, density 1.4g/cm3Sulfuric acid, acid addition time 11-13min, and
Lasting stirring;(4) water cooling: when cream temperature is 55-58 DEG C, start circulating water cooling;(5) air-cooled: when cream temperature is between 65-75 DEG C
When, start air cooling;(6) go out cream: the mixing time after acid adding is more than or equal to 7min, and paste outer temperature is less than or equal to 48 DEG C, out
Paste density when cream is 4.4-4.5g/cm3;
Raw material in the step (1) is grouped as by the group of following parts by weight: 990-1010 parts of lead powder, additive 4.7-5.0
Part, 1.4-2 parts of lead orthoplumbate, 20-24 parts of fecula drench sour 8-10 parts of powder;
The fecula is the positive lead plaster of recycling or the lead powder made of positive raw plate dries pulverizing sieving that gives up;
The sour powder of the leaching is made of the lead sulfate of 40%-60%, remaining ingredient is lead.
2. anode mixing paste technology according to claim 1, it is characterised in that: the additive is staple fiber, three oxidations
Two antimony, stannous sulfate and nano-graphite.
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CN106654395A (en) * | 2016-12-28 | 2017-05-10 | 双登集团股份有限公司 | Method for lowering floating powder from surface of electrode plate of lead-acid storage battery |
CN109273716B (en) * | 2018-08-16 | 2020-04-03 | 天能电池集团股份有限公司 | Long-life lead storage battery and preparation method thereof |
CN110707295A (en) * | 2019-09-16 | 2020-01-17 | 天能电池(芜湖)有限公司 | High temperature and paste technology at 90 DEG C |
CN111106314B (en) * | 2019-11-28 | 2022-09-20 | 安徽力普拉斯电源技术有限公司 | High-temperature paste mixing method for positive electrode lead paste of lead-acid storage battery |
CN112563460B (en) * | 2020-12-10 | 2023-01-17 | 淄博火炬能源有限责任公司 | Low-temperature power battery and preparation method thereof |
CN114597397B (en) * | 2021-11-29 | 2023-10-24 | 超威电源集团有限公司 | Paste mixing process for lead paste of lead-acid storage battery |
Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1395330A (en) * | 2001-07-09 | 2003-02-05 | 保定金风帆蓄电池有限公司 | Preparation method of positive plate lead paste of lead-acid battery |
JP2007220644A (en) * | 2006-01-17 | 2007-08-30 | Furukawa Battery Co Ltd:The | Method of manufacturing lead acid battery electrode plate |
JP2009048800A (en) * | 2007-08-15 | 2009-03-05 | Shin Kobe Electric Mach Co Ltd | Manufacturing method for paste type positive electrode plate |
CN102244261A (en) * | 2010-05-20 | 2011-11-16 | 江苏双登集团有限公司 | Anode active material of valve-regulated sealed lead acid battery for communication and preparation and curing method thereof |
CN102354751A (en) * | 2011-08-24 | 2012-02-15 | 天能电池集团(安徽)有限公司 | Formula and preparation method of high energy storage lead-acid battery lead paste |
CN102664256A (en) * | 2012-04-27 | 2012-09-12 | 天能电池集团有限公司 | Anode lead plaster of power lead-acid storage battery polar plate |
CN103247827A (en) * | 2013-04-07 | 2013-08-14 | 天能电池(芜湖)有限公司 | Composite additive of lead-acid storage battery |
CN104167546A (en) * | 2014-05-21 | 2014-11-26 | 河南超威电源有限公司 | Lead paste for battery starting/stopping, and preparation method thereof |
CN104241609A (en) * | 2014-07-01 | 2014-12-24 | 超威电源有限公司 | Vacuum paste mixing process of lead-acid power battery |
CN105280916A (en) * | 2015-02-11 | 2016-01-27 | 济源市万洋绿色能源有限公司 | Composite paste for inner formation of lead-acid storage battery |
-
2016
- 2016-06-30 CN CN201610499741.8A patent/CN106099049B/en active Active
Patent Citations (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1395330A (en) * | 2001-07-09 | 2003-02-05 | 保定金风帆蓄电池有限公司 | Preparation method of positive plate lead paste of lead-acid battery |
JP2007220644A (en) * | 2006-01-17 | 2007-08-30 | Furukawa Battery Co Ltd:The | Method of manufacturing lead acid battery electrode plate |
JP2009048800A (en) * | 2007-08-15 | 2009-03-05 | Shin Kobe Electric Mach Co Ltd | Manufacturing method for paste type positive electrode plate |
CN102244261A (en) * | 2010-05-20 | 2011-11-16 | 江苏双登集团有限公司 | Anode active material of valve-regulated sealed lead acid battery for communication and preparation and curing method thereof |
CN102354751A (en) * | 2011-08-24 | 2012-02-15 | 天能电池集团(安徽)有限公司 | Formula and preparation method of high energy storage lead-acid battery lead paste |
CN102664256A (en) * | 2012-04-27 | 2012-09-12 | 天能电池集团有限公司 | Anode lead plaster of power lead-acid storage battery polar plate |
CN103247827A (en) * | 2013-04-07 | 2013-08-14 | 天能电池(芜湖)有限公司 | Composite additive of lead-acid storage battery |
CN104167546A (en) * | 2014-05-21 | 2014-11-26 | 河南超威电源有限公司 | Lead paste for battery starting/stopping, and preparation method thereof |
CN104241609A (en) * | 2014-07-01 | 2014-12-24 | 超威电源有限公司 | Vacuum paste mixing process of lead-acid power battery |
CN105280916A (en) * | 2015-02-11 | 2016-01-27 | 济源市万洋绿色能源有限公司 | Composite paste for inner formation of lead-acid storage battery |
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