CN1260846C - Internal chemical synthetic process for colloidal battery - Google Patents
Internal chemical synthetic process for colloidal battery Download PDFInfo
- Publication number
- CN1260846C CN1260846C CNB031590187A CN03159018A CN1260846C CN 1260846 C CN1260846 C CN 1260846C CN B031590187 A CNB031590187 A CN B031590187A CN 03159018 A CN03159018 A CN 03159018A CN 1260846 C CN1260846 C CN 1260846C
- Authority
- CN
- China
- Prior art keywords
- battery
- electrolyte
- battery case
- internal formation
- colloidal
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims description 16
- 239000003792 electrolyte Substances 0.000 claims abstract description 15
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 claims abstract description 7
- 239000000084 colloidal system Substances 0.000 claims description 8
- 238000012856 packing Methods 0.000 claims description 4
- 239000002253 acid Substances 0.000 abstract description 13
- 238000005516 engineering process Methods 0.000 abstract description 12
- 230000005484 gravity Effects 0.000 abstract description 2
- 238000005192 partition Methods 0.000 abstract 4
- 239000008151 electrolyte solution Substances 0.000 abstract 1
- 239000012530 fluid Substances 0.000 abstract 1
- 238000007789 sealing Methods 0.000 abstract 1
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 description 2
- 238000003556 assay Methods 0.000 description 2
- 230000000295 complement effect Effects 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052938 sodium sulfate Inorganic materials 0.000 description 1
- 235000011152 sodium sulphate Nutrition 0.000 description 1
Images
Classifications
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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
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
The present invention relates to an internal formation technology for a colloidal battery, particularly to an internal formation technology for a colloidal lead-acid accumulator in a manufacturing process. Positive pole plates, negative pole plates and partition plates of a battery are combined into single partition pole groups which are arranged in a battery case, connected and processed through cover sealing, and pass a test; an electrolyte of 1.32 g/cm<3> is added to the battery case, charged and discharged until battery voltage is OV, and superfluous electrolyte is poured out; prepared colloidal fluid (of which a patent is already applied)with apparent specific gravity of 1.13 g/cm<3> is poured into a battery jar and processed through the technologies of charging, discharge, group matching and recharging, and then passes a test according to a standard. In the present invention, the actual acid use quantity of battery pole groups is controlled, so that the acid quantity of each single partition pole group matches with the capacity of the partition pole group, battery salinization caused by incontrollable battery electrolytic solution is prevented, and battery cycle life is greatly extended.
Description
Technical field:
The present invention relates to a kind of internal formation process of colloid battery, the internal formation process in particularly a kind of gelled lead acid battery manufacturing process, it belongs to industrial battery technology field.
Background technology:
Internal formation process in the gelled lead acid battery manufacturing process is meant carrying out the technology of charge and discharge process in the battery pot shell, internal formation process flow process of the prior art is seen Fig. 1, be combined as positive and negative pole plate, dividing plate single by the instrument folder every utmost point group, the battery case of packing into is interior to connect every list every utmost point group rear seal-cover, has promptly finished assembly technology after the assay was approved; Be that to mix apparent gravity that the back produces be that 1.40 mixture pours in the battery case and charges for 1.34 sulfuric acid, phosphoric acid, white carbon black, sodium sulphate again with proportion; Behind overdischarge, combo, charge technology, roll off the production line by being up to the standards at last again.Above-mentioned technological process, because the every list of inside battery comprises the suction acid rate of dividing plate pole plate and all there are differences between utmost point group, utmost point group be there are differences with the acid amount, after quantitative colloidal electrolyte is added utmost point group, can produce between the utmost point group uneven with the acid amount, battery causes salinization easily when the acid amount is not enough, and capacity reduces, and the life-span reduces.
Summary of the invention:
Technical problem to be solved by this invention provides a kind of every list of battery that makes and is complementary every acid amount and utmost point group capacity, makes the acid of using between the utmost point group measure balance, and can improve the internal formation process of the colloid battery of battery cycle life effectively.
The present invention solves the problems of the technologies described above the technical scheme that is adopted: the internal formation process of this colloid battery may further comprise the steps:
A, positive and negative pole plate, dividing plate are combined as single, connect every list in the battery case of packing into every utmost point group rear seal-cover every utmost point group;
C, charging, discharge, combo, recharge;
D, be up to the standards and roll off the production line;
It is characterized in that also being provided with step b between described step a and the step c, step b is: add electrolyte, be discharged to 0V after the charging again, remove unnecessary electrolyte, the colloidal solution that configures is poured into battery case.
The described adding electrolyte of step b of the present invention is to add 1.32g/cm
3Electrolyte.
Step b of the present invention is described, and the colloidal solution that configures is poured into battery case is that the proportion that will configure is 1.13g/cm
3Colloidal solution pour into battery case.
The present invention compared with prior art, have the following advantages and effect: use technology of the present invention, can control effectively with the acid amount to battery electrode group is actual, when battery discharge during to 0V, battery electrode group all utilizes the sulfuric acid that is over, remove unnecessary electrolyte after, the every list of battery is complementary every acid amount and utmost point group capacity, preventing that battery electrolyte is out of control causes the battery salinization, and has improved the cycle life of battery greatly.
Description of drawings:
Fig. 1 is the internal formation process flow chart of existing colloid battery.
Fig. 2 is a process chart of the present invention.
Embodiment:
Referring to Fig. 2, the present invention is combined as list every utmost point group with positive and negative pole plate and dividing plate by the instrument folder, connects every list in the battery case of packing into every utmost point group rear seal-cover, has promptly finished assembly technology after the assay was approved; Add 1.32g/cm then
3Electrolyte, when after overcharging, being discharged to cell voltage again and being 0V, remove unnecessary electrolyte, be 1.13g/cm with the proportion that configures
3Colloidal solution pour into battery case; Again through overcharge, discharge, combo, recharge technology after, roll off the production line after qualified by standard test.
Claims (3)
1, a kind of internal formation process of colloid battery may further comprise the steps:
A, positive and negative pole plate, dividing plate are combined as single, connect every list in the battery case of packing into every utmost point group rear seal-cover every utmost point group;
C, charging, discharge, combo, recharge;
D, be up to the standards and roll off the production line;
It is characterized in that: also be provided with step b between described step a and the step c, step b is: add electrolyte, be discharged to 0V after the charging again, remove unnecessary electrolyte, the colloidal solution that configures is poured into battery case.
2, the internal formation process of colloid battery according to claim 1 is characterized in that: the described adding electrolyte of step b is to add 1.32g/cm
3Electrolyte.
3, the internal formation process of colloid battery according to claim 1 is characterized in that: step b is described, and the colloidal solution that configures is poured into battery case is that the proportion that will configure is 1.13g/cm
3Colloidal solution pour into battery case.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031590187A CN1260846C (en) | 2003-09-11 | 2003-09-11 | Internal chemical synthetic process for colloidal battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031590187A CN1260846C (en) | 2003-09-11 | 2003-09-11 | Internal chemical synthetic process for colloidal battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1564366A CN1564366A (en) | 2005-01-12 |
| CN1260846C true CN1260846C (en) | 2006-06-21 |
Family
ID=34472728
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB031590187A Expired - Lifetime CN1260846C (en) | 2003-09-11 | 2003-09-11 | Internal chemical synthetic process for colloidal battery |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1260846C (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100369299C (en) * | 2005-12-30 | 2008-02-13 | 浙江南都电源动力股份有限公司 | Forming method of lead-acid battery electrode plate transplantation |
| CN101853958B (en) * | 2010-06-04 | 2013-11-13 | 山东圣阳电源股份有限公司 | Tubular colloidal battery and manufacturing technology thereof |
| CN102569908A (en) * | 2012-01-18 | 2012-07-11 | 广西大学 | Method for assembling valve-control sealed type maintenance-free lead acid storage battery |
| CN103700892B (en) * | 2013-12-23 | 2016-05-11 | 扬州市永达电源有限公司 | Maitenance-free colloid lead-acid accumulator is efficiently internalized into charge technology |
| CN106025390B (en) * | 2016-08-08 | 2019-06-14 | 淄博火炬能源有限责任公司 | The production technology of tubular colloidal battery |
-
2003
- 2003-09-11 CN CNB031590187A patent/CN1260846C/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| CN1564366A (en) | 2005-01-12 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHEJIANG HAIJIU BATTERY CO., LTD. Free format text: FORMER OWNER: CHEN GANG Effective date: 20080704 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20080704 Address after: New town industrial zone, Zhejiang, Deqing County Patentee after: ZHEJIANG HAIJIU BATTERY Co.,Ltd. Address before: Zhejiang, Hangzhou Province mid level stone village long sea Battery Co., Ltd. Patentee before: Chen Gang |
|
| C56 | Change in the name or address of the patentee |
Owner name: ZHEJIANG PROV HAIJIU BATTERY CO., LTD. Free format text: FORMER NAME: ZHEJIANG PROVINCE HAIJIU BATTERY CO., LTD. |
|
| CP03 | Change of name, title or address |
Address after: New town industrial zone, Zhejiang, Deqing County Patentee after: ZHEJIANG HAIJIU BATTERY Co.,Ltd. Address before: New town industrial zone, Zhejiang, Deqing County Patentee before: ZHEJIANG HAIJIU BATTERY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20170209 Address after: 313103 Changxin economic and Technological Development Zone, Zhejiang City, South industrial functional area Patentee after: CHANGING YIDING POWER SUPPLY CO.,LTD. Address before: 313201 Zhejiang province Deqing County New Town Industrial Park Patentee before: ZHEJIANG HAIJIU BATTERY Co.,Ltd. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20201216 Address after: 310018 1st and 2nd floors, building 2, No. 161, No. 17 street, Baiyang street, Hangzhou Economic and Technological Development Zone, Zhejiang Province Patentee after: Hangzhou Haijiu Battery Co.,Ltd. Address before: 313103 Chengnan industrial functional zone, Changxing Economic and Technological Development Zone, Huzhou City, Zhejiang Province Patentee before: CHANGING YIDING POWER SUPPLY Co.,Ltd. |
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| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20060621 |