JPS603871A - Lead-acid battery - Google Patents
Lead-acid batteryInfo
- Publication number
- JPS603871A JPS603871A JP58113421A JP11342183A JPS603871A JP S603871 A JPS603871 A JP S603871A JP 58113421 A JP58113421 A JP 58113421A JP 11342183 A JP11342183 A JP 11342183A JP S603871 A JPS603871 A JP S603871A
- Authority
- JP
- Japan
- Prior art keywords
- lead
- silica
- sulfuric acid
- powder
- dilute sulfuric
- 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.)
- Pending
Links
Classifications
-
- 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
- H01M4/36—Selection of substances as active materials, active masses, active liquids
- H01M4/48—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides
- H01M4/56—Selection of substances as active materials, active masses, active liquids of inorganic oxides or hydroxides of lead
-
- 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
Abstract
Description
【発明の詳細な説明】
本発明は電解液に希硫酸と無水珪酸等とを混合してゲル
化させたゲル電解液を使用()、正極板にクラッド式極
板を用いた3))蓄電池の改良にIWJりるものCある
。Detailed Description of the Invention The present invention uses a gel electrolyte solution made by mixing dilute sulfuric acid, silicic acid anhydride, etc. to form a gel, and uses a clad type electrode plate for the positive electrode plate 3)) Storage battery IWJ Rirmono C is an improvement on this.
従来、無漏液形あるいは密閉形1()蓄電池においCは
、電解液に希硫酸と無水珪酸等を混合してゲル化さけた
ゲル電解液が使用されている。このような希硫酸を無水
珪酸等を用いてゲル化させたゲルTi解液を使用した場
合、ペースト式J3よびクラッド式のいずれの極板を用
いた鉛蓄電池でも、無水珪酸の微粉末は極板の活物質細
孔内に入らず、希rIi!l醸のみが活1カ賀内に浸透
する。したかっ−C充電中に発生したガスによって細孔
内の希硫酸が極板外に押し出され、これらはゲル電解液
と分離して離漿液どなってグル電解液の上部に溜り、液
漏れの原因になるどいった欠点があった。ベースト式極
板を用いた鉛蓄電池ではそれに対−4る良好な対策が提
案されていくTいが、本発明はクラッド式極板を用いた
鉛蓄電池において、このようイf欠点を除去すると共に
、従来よりf>71ぐれた容量をイjする電池を提供J
るものである。その要旨と4るところは、従来、ブ」−
ブに鉛粉を充1眞しでいたのに対して、鉛粉と無水珪酸
微粉末(以後、シリカ粉末という)を充In する、即
ち、正(セ活物質中に無水珪酸微粉末を混入することに
ある。このように覆ることによって、正極活物質細孔内
にあらかじめシリカ粉末が存在Jるのひ、たとえゲル電
解液が濾過されて希硫酸のみが活物質の細孔内に浸透し
てきても該シリカ粉末によって吸収されるので、従来の
ように充電時に活物質細孔内から遊離の希硫酸が押し出
されて離漿液になることはない。Conventionally, in non-leak type or sealed type 1() storage batteries, a gel electrolyte solution prepared by mixing dilute sulfuric acid, anhydrous silicic acid, etc. with the electrolyte solution to avoid gelation has been used. When using a gel Ti solution made by gelling such dilute sulfuric acid with silicic acid anhydride, fine powder of silicic anhydride is extremely It does not enter the active material pores of the plate, and the dilute rIi! Only 1 brewing permeates into Katsuichi Kakanai. The dilute sulfuric acid in the pores is pushed out of the electrode plate by the gas generated during charging, which separates from the gel electrolyte and forms a syneresis fluid that accumulates at the top of the gel electrolyte, causing leakage. What kind of flaws were there that caused it? Although good countermeasures have been proposed for lead-acid batteries using base-type electrode plates, the present invention eliminates these drawbacks in lead-acid batteries using clad-type electrode plates. , provides a battery with a capacity greater than conventional ones by f > 71.
It is something that The main point and four points are that
In contrast to the previous method in which the lead powder was filled with lead powder, it was filled with lead powder and anhydrous silicic acid fine powder (hereinafter referred to as silica powder). By covering in this way, even if silica powder is already present in the pores of the positive electrode active material, even if the gel electrolyte is filtered, only dilute sulfuric acid will penetrate into the pores of the active material. However, the silica powder absorbs the free dilute sulfuric acid, so that free dilute sulfuric acid is not pushed out from the pores of the active material and becomes a synergic fluid during charging, unlike in the conventional case.
次に具体例をもって詳細に1L12明する。酸化度70
%の鉛粉I Kqに対して、重石パーセン1−で8%の
シリカ粉末を添加し、これをチューブに充填し−C作製
したクラッド式極板を用いて無水珪酸を重石パーレン1
〜で10%含む比重1.28の希硫酸を注入した公称容
1200At+の本発明による鉛蓄電池と、従来からの
鉛粉を充填したクラッド式極板を用いて前記ど同じ電解
液を注入した同容量の従来形鉛蓄電池とをそれぞれ作製
し、これらの電池について初充電後の剛漿液吊おにび初
期容量を比較した。Next, 1L12 will be explained in detail using a specific example. Oxidation degree 70
% of lead powder I Kq, 8% silica powder is added with a weight of 1-1, and this is filled into a tube.
A lead-acid battery according to the present invention having a nominal capacity of 1200 At+ was injected with dilute sulfuric acid with a specific gravity of 1.28 containing 10% of sulfuric acid, and the same electrolyte was injected with the same electrolyte using a conventional clad plate filled with lead powder. A conventional lead-acid battery with a different capacity was prepared, and the initial capacity of these batteries after the first charge was compared.
その結果を表1に示す。なお、表1では、いずれについ
ても従来品を100とした時の比率で示した。The results are shown in Table 1. In addition, in Table 1, all are shown as ratios when the conventional product is set as 100.
表 1
表1より明らかなように、本発明品においては、前述し
Iこように活物質細孔内に存在J°るシリカ粉末によつ
−C遊離の8硫酸が吸収されるのぐ、離漿液はほとんど
生成しなかった。また容量についても、性能が大幅に改
善された。これは活物質細孔内にもシリカ粉末が存在し
−C希硫酸を吸収保持していて、シリカd3 J:び希
硫酸の濃度が細孔内で均一でしかも電解液層につながり
があるため、放電時の硫酸の供給がスムーズになるため
である。Table 1 As is clear from Table 1, in the product of the present invention, as the -C free 8-sulfuric acid is absorbed by the silica powder existing in the pores of the active material as described above, Almost no syneresis fluid was produced. In terms of capacity, performance has also been significantly improved. This is because silica powder exists within the pores of the active material and absorbs and retains -C dilute sulfuric acid, and the concentration of silica d3 J: and dilute sulfuric acid is uniform within the pores and is connected to the electrolyte layer. This is because the supply of sulfuric acid during discharge becomes smooth.
以上のように本発明に基づき、ゲル電解液を使用したク
ラッド式鉛蓄電池におい(、正極活物質中に無水珪酸微
粉末を混入することにより、従来のこの種鉛蓄電池の欠
点であった離漿液の生成をなくし、液漏れない安定した
鉛蓄電池が行られると共に、従来品に較べて性能も大幅
に改善できる。As described above, based on the present invention, in a clad lead-acid battery using a gel electrolyte (by mixing anhydrous silicic acid fine powder into the positive electrode active material, syneresis liquid, which has been a drawback of conventional lead-acid batteries of this type) This eliminates the formation of lead-acid batteries, which are stable and do not leak, and also significantly improves performance compared to conventional products.
Claims (1)
112を用い、且つif正極板クラッド式極板を用いた
1()蓄電池におい(,11極活物質中に無水珪酸微粉
末を混入したことを特徴とする鉛蓄電池。Gel electrolysis formed with anhydrous silicon VU cap and dilute sulfuric acid in the electrolyte)
112, and a 1() storage battery using an IF positive electrode plate clad type electrode plate (11) A lead-acid battery characterized in that an anhydrous silicic acid fine powder is mixed in the electrode active material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58113421A JPS603871A (en) | 1983-06-22 | 1983-06-22 | Lead-acid battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58113421A JPS603871A (en) | 1983-06-22 | 1983-06-22 | Lead-acid battery |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS603871A true JPS603871A (en) | 1985-01-10 |
Family
ID=14611812
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58113421A Pending JPS603871A (en) | 1983-06-22 | 1983-06-22 | Lead-acid battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS603871A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63150864A (en) * | 1986-12-12 | 1988-06-23 | Yuasa Battery Co Ltd | Enclosed lead storage battery |
JPH01102860A (en) * | 1987-10-15 | 1989-04-20 | Japan Storage Battery Co Ltd | Sealed lead-acid battery |
US7682738B2 (en) | 2002-02-07 | 2010-03-23 | Kvg Technologies, Inc. | Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it |
-
1983
- 1983-06-22 JP JP58113421A patent/JPS603871A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63150864A (en) * | 1986-12-12 | 1988-06-23 | Yuasa Battery Co Ltd | Enclosed lead storage battery |
JPH01102860A (en) * | 1987-10-15 | 1989-04-20 | Japan Storage Battery Co Ltd | Sealed lead-acid battery |
US7682738B2 (en) | 2002-02-07 | 2010-03-23 | Kvg Technologies, Inc. | Lead acid battery with gelled electrolyte formed by filtration action of absorbent separators and method for producing it |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH09147869A (en) | Lead-acid battery | |
JPS603871A (en) | Lead-acid battery | |
JP3511949B2 (en) | Sealed lead-acid battery | |
JPH0696793A (en) | Manufacture of sealed lead-acid battery | |
JPS5882472A (en) | Lead storage battery and manufacture thereof | |
JPS59177863A (en) | Gel type lead-acid battery | |
JP2559610B2 (en) | Method for manufacturing sealed lead acid battery | |
JPH0883622A (en) | Sealed lead-acid battery | |
JPS6030064A (en) | Manufacture of sealed type lead-acid battery | |
JP2006185743A (en) | Control valve type lead-acid battery | |
JP2958790B2 (en) | Sealed lead-acid battery | |
JP2573094B2 (en) | Manufacturing method of sealed lead-acid battery | |
JP2815439B2 (en) | Sealed lead-acid battery | |
JPH02216760A (en) | Zinc alkaline battery | |
JP2581237B2 (en) | Manufacturing method of sealed lead-acid battery | |
JPS62168349A (en) | Anode plate for enclosed lead storage battery | |
JP2952374B2 (en) | Sealed lead-acid battery | |
JPS59177862A (en) | Gel type lead-acid battery | |
JPS6313261A (en) | Charging method for lead-acid battery | |
JPH08298133A (en) | Sealed lead acid battery | |
JPS60249243A (en) | Positive plate for sealed storage battery | |
JPS5873958A (en) | Manufacture of alkaline battery | |
JPS6324303B2 (en) | ||
JPS58121564A (en) | Manufacturing method of button type alkaline battery | |
JPH03201363A (en) | Enclosed type lead storage battery |