JPH0249355A - Manufacture of sealed lead-acid battery - Google Patents
Manufacture of sealed lead-acid batteryInfo
- Publication number
- JPH0249355A JPH0249355A JP63201408A JP20140888A JPH0249355A JP H0249355 A JPH0249355 A JP H0249355A JP 63201408 A JP63201408 A JP 63201408A JP 20140888 A JP20140888 A JP 20140888A JP H0249355 A JPH0249355 A JP H0249355A
- Authority
- JP
- Japan
- Prior art keywords
- lead
- active material
- lead oxide
- cycle life
- battery
- 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.)
- Granted
Links
- 239000002253 acid Substances 0.000 title claims description 10
- 238000004519 manufacturing process Methods 0.000 title claims description 4
- 229910000464 lead oxide Inorganic materials 0.000 claims abstract description 3
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims abstract description 3
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 claims abstract description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 2
- 239000007774 positive electrode material Substances 0.000 abstract description 9
- 230000006866 deterioration Effects 0.000 abstract description 3
- 239000003792 electrolyte Substances 0.000 abstract description 3
- 230000006835 compression Effects 0.000 abstract description 2
- 238000007906 compression Methods 0.000 abstract description 2
- XMFOQHDPRMAJNU-UHFFFAOYSA-N lead(ii,iv) oxide Chemical compound O1[Pb]O[Pb]11O[Pb]O1 XMFOQHDPRMAJNU-UHFFFAOYSA-N 0.000 abstract 3
- 239000011149 active material Substances 0.000 abstract 2
- 239000000843 powder Substances 0.000 abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 6
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
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
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/34—Gastight accumulators
- H01M10/342—Gastight lead accumulators
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Secondary Cells (AREA)
- Battery Electrode And Active Subsutance (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は密閉型鉛蓄電池の製造方法に関するものである
。DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to a method of manufacturing a sealed lead acid battery.
従来の技術
従来、鉛蓄電池において正極活物質中に鉛丹を添加する
ことにより正極活物質の利用率を向上させることが可能
であり、第3図に示すような初期における容量の増加が
認められた。Aは鉛丹無添加、C,Dは鉛丹を40wt
%添加した電池の25’C,0,25CAによる放電時
間と端子電圧との関係図である。Conventional technology Conventionally, in lead-acid batteries, it has been possible to improve the utilization rate of the positive electrode active material by adding red lead to the positive electrode active material, and an increase in initial capacity as shown in Figure 3 has been observed. Ta. A has no red lead added, C and D have 40wt red lead.
FIG. 3 is a diagram showing the relationship between the discharge time and the terminal voltage at 25'C, 0.25CA for a battery containing 0.0% of the oxidation rate.
発明が解決しようとする課題
鉛丹を添加した正極板を用いた鉛蓄電池について、従来
の群圧では正極活物質の微細化が原因で、第2図のCに
示すようなサイクル寿命の早期低下をきたすという問題
点があった。Problems to be Solved by the Invention Regarding lead-acid batteries using a positive electrode plate containing red lead, with conventional group pressure, the cycle life decreases prematurely as shown in C in Figure 2 due to the miniaturization of the positive electrode active material. There was a problem in that it caused
電池A、C,Dの充電は定電圧充電で7.35V/Ma
x 0.4CAで6時間充電、また放電は25℃で0
.25CA15.25Vendとした。Batteries A, C, and D are charged at a constant voltage of 7.35V/Ma.
Charging for 6 hours at x 0.4CA, and discharging at 25℃
.. 25CA15.25Vend.
本発明の目的は上記のような問題点を解決し、正極活物
質に鉛丹を添加することによる利用率の向上を維持した
まま、サイクル寿命の早期低下を抑制することのできる
密閉型鉛蓄電池を提供しようとするものである。The purpose of the present invention is to solve the above-mentioned problems, and to provide a sealed lead-acid battery that can suppress early deterioration of cycle life while maintaining the improvement in utilization rate by adding red lead to the positive electrode active material. This is what we are trying to provide.
課題を解決するための手段
上記目的を達成するために本発明は、正極格子に塗り込
むペーストとして、鉛及び鉛酸化物からなる鉛粉中に鉛
丹な20〜40wt%混合したべ−ストを用い、電槽内
にこの正極板を備えた極板群を組み込み、電解液(希硫
酸)を注液した後に、極板及びセパレータに35にg/
drn”以上で55 Kg/dは以下の荷重がかかるよ
うな群圧を与える密閉型鉛蓄電池の製造方法とした。Means for Solving the Problems In order to achieve the above objects, the present invention uses a base containing 20 to 40 wt% of lead mixed in lead powder made of lead and lead oxide as a paste to be applied to the positive electrode grid. After installing the electrode plate group including this positive electrode plate in a battery case and pouring electrolyte (dilute sulfuric acid) into the electrode plate and separator, 35 g/
The method for producing a sealed lead-acid battery was such that a group pressure of 55 Kg/d or less was applied above 55 Kg/d.
作用
本発明では上記のように電槽内の極板群及びセパレータ
に35〜55 Kg/drn”以下の荷重がかかるよう
群圧を与えたので、鉛丹を正極活物質に添加したことに
よる利用率の向上を維持したまま、微細化した正極活物
質の微細化をセパレータの圧縮比を高めることにより阻
止し、サイクル寿命の早期低下を抑制することとなる。Function In the present invention, as described above, a group pressure is applied so that a load of 35 to 55 Kg/drn is applied to the electrode plate group and separator in the battery case. By increasing the compression ratio of the separator, it is possible to prevent the fineness of the positive electrode active material from becoming fine while maintaining the improvement in the ratio, thereby suppressing an early decrease in the cycle life.
実施例
6V6.5Ah (20HR)タイプの密閉型鉛蓄電池
において、第1表に示すようなA、B、C,D、E、F
の6種類の密閉型鉛蓄電池を試作し、サイクル寿命試験
を実施した。またA、C1Dの3種類の密閉型鉛蓄電池
については、0.25CAでの容量試験を実施した後、
サイクル寿命メ験を実施した。寿命は初期容量の50%
以下になった時をとった。正極板、負極板の厚さは、全
ての電池について同一であり、正極板厚み3.25mm
、負極板厚み1.89mmで、電槽幅の内1jは27.
4mmである。セパレータは繊維径0.7μmをt体と
した目付用m I 55 g / rrH”のガラス繊
維セパレータを2枚重ねて使用した。負極板については
同一仕様のものを使用した。Example 6 In a V6.5Ah (20HR) type sealed lead-acid battery, A, B, C, D, E, F as shown in Table 1
Six types of sealed lead-acid batteries were prototyped and cycle life tests were conducted. In addition, for the three types of sealed lead acid batteries A and C1D, after carrying out a capacity test at 0.25CA,
A cycle life test was conducted. Lifespan is 50% of initial capacity
I took the time when it became below. The thickness of the positive electrode plate and negative electrode plate is the same for all batteries, and the positive electrode plate thickness is 3.25 mm.
, the negative electrode plate thickness is 1.89 mm, and 1j of the battery case width is 27.
It is 4mm. The separator used was a stack of two glass fiber separators with a fiber diameter of 0.7 μm and a fabric weight of m I 55 g/rrH”.As for the negative electrode plate, one with the same specifications was used.
く第1表〉
第1表においてセパレータ厚さは乾燥状態で20にg/
dm”加圧時の厚さを、セパレータにかかる荷重は、電
池として組み立てられた後、電解液(希硫酸)を含んだ
状態のセパレータに加わる荷重を表わしている。Table 1 In Table 1, the separator thickness in the dry state is 20 g/
dm'' thickness when pressurized, and the load applied to the separator represents the load applied to the separator containing electrolyte (dilute sulfuric acid) after being assembled as a battery.
各電池の初期容量試験を第3図に、サイクル寿命試験の
結果を第1図、第2図に示す。The initial capacity test of each battery is shown in FIG. 3, and the results of the cycle life test are shown in FIGS. 1 and 2.
第2図より本発明の実施例の電池りは容量が大きく、サ
イクル寿命特性も優れていることがわかる。From FIG. 2, it can be seen that the battery according to the example of the present invention has a large capacity and excellent cycle life characteristics.
第1図より電池内において硫酸を含んだ状態のセパレー
タに35 Kg/drn”以上の荷重がかかっていれば
同様の効果が得られるが、電池の組立工程上、その上限
は55にg/drn″以下であることが必要である。From Figure 1, the same effect can be obtained if a load of 35 kg/drn or more is applied to the separator containing sulfuric acid in the battery, but due to the battery assembly process, the upper limit is 55 g/drn. ″ or less.
発明の効果
上記のように本発明によれば、正極板のペーストに鉛丹
を20〜40wL%混合し、極板群にがかる群圧を35
〜55 Kg/dm”とすることにより、正極活物質の
利用率向上を維持すると同時に、正極活物質の微細化に
ともなうサイクル寿命の早期低下を抑制することができ
た。Effects of the Invention As described above, according to the present invention, 20 to 40 wL% of red lead is mixed into the paste of the positive electrode plate, and the group pressure applied to the electrode plate group is reduced to 35%.
~55 Kg/dm'', it was possible to maintain an improvement in the utilization rate of the positive electrode active material, and at the same time, it was possible to suppress an early decrease in the cycle life due to the miniaturization of the positive electrode active material.
第1図は電池内でセパレータにかかる荷重とサイクル寿
命の関係図、第2図はサイクル数と放電持続時間との関
係図、第3図は初期容量試験の結果を示す図、第4図は
荷重と本実験で使用したセパレータの厚さとの関係図で
ある。Figure 1 is a diagram showing the relationship between the load applied to the separator in the battery and cycle life, Figure 2 is a diagram showing the relationship between the number of cycles and discharge duration, Figure 3 is a diagram showing the results of the initial capacity test, and Figure 4 is a diagram showing the relationship between the number of cycles and discharge duration. FIG. 3 is a diagram showing the relationship between load and the thickness of the separator used in this experiment.
Claims (1)
化物からなる鉛粉中に鉛丹を20〜40wt%混合した
ペーストを用い、電槽内に極板群を組み込み、電解液(
希硫酸)を注液した後に、極板及びセパレータに35K
g/dm^2以上で55Kg/dm^2以下の荷重がか
かるような群圧を与えることを特徴とする密閉型鉛蓄電
池の製造方法。(1) As the paste to be applied to the positive electrode grid, use a paste containing 20 to 40 wt% of red lead mixed into lead powder made of lead and lead oxide.
After injecting dilute sulfuric acid), heat the electrode plate and separator to 35K.
A method for manufacturing a sealed lead-acid battery, characterized by applying a group pressure such that a load of 55 kg/dm^2 or more is applied to the battery.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63201408A JP2721514B2 (en) | 1988-08-11 | 1988-08-11 | Manufacturing method of sealed lead-acid battery |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63201408A JP2721514B2 (en) | 1988-08-11 | 1988-08-11 | Manufacturing method of sealed lead-acid battery |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0249355A true JPH0249355A (en) | 1990-02-19 |
JP2721514B2 JP2721514B2 (en) | 1998-03-04 |
Family
ID=16440593
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63201408A Expired - Lifetime JP2721514B2 (en) | 1988-08-11 | 1988-08-11 | Manufacturing method of sealed lead-acid battery |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2721514B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995015584A1 (en) * | 1993-12-03 | 1995-06-08 | Bipolar Power Corporation | Bipolar battery construction |
JP2002093459A (en) * | 2000-09-14 | 2002-03-29 | Matsushita Electric Ind Co Ltd | Sealed lead-acid battery and its manufacturing method |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009055020A (en) * | 2007-07-31 | 2009-03-12 | L'air Liquide-Sa Pour L'etude & L'exploitation Des Procedes Georges Claude | Improved alkaline chemical for post-cmp cleaning |
JP2009081475A (en) * | 2009-01-22 | 2009-04-16 | Fujitsu Microelectronics Ltd | Method of manufacturing semiconductor device |
JP2013004910A (en) * | 2011-06-21 | 2013-01-07 | Disco Abrasive Syst Ltd | Processing method of wafer having embedded copper electrode |
-
1988
- 1988-08-11 JP JP63201408A patent/JP2721514B2/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009055020A (en) * | 2007-07-31 | 2009-03-12 | L'air Liquide-Sa Pour L'etude & L'exploitation Des Procedes Georges Claude | Improved alkaline chemical for post-cmp cleaning |
JP2009081475A (en) * | 2009-01-22 | 2009-04-16 | Fujitsu Microelectronics Ltd | Method of manufacturing semiconductor device |
JP2013004910A (en) * | 2011-06-21 | 2013-01-07 | Disco Abrasive Syst Ltd | Processing method of wafer having embedded copper electrode |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995015584A1 (en) * | 1993-12-03 | 1995-06-08 | Bipolar Power Corporation | Bipolar battery construction |
JP2002093459A (en) * | 2000-09-14 | 2002-03-29 | Matsushita Electric Ind Co Ltd | Sealed lead-acid battery and its manufacturing method |
JP4719962B2 (en) * | 2000-09-14 | 2011-07-06 | パナソニック株式会社 | Manufacturing method of sealed lead-acid battery |
Also Published As
Publication number | Publication date |
---|---|
JP2721514B2 (en) | 1998-03-04 |
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