WO2014076883A1 - Lead-acid cell - Google Patents
Lead-acid cell Download PDFInfo
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- WO2014076883A1 WO2014076883A1 PCT/JP2013/006224 JP2013006224W WO2014076883A1 WO 2014076883 A1 WO2014076883 A1 WO 2014076883A1 JP 2013006224 W JP2013006224 W JP 2013006224W WO 2014076883 A1 WO2014076883 A1 WO 2014076883A1
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/08—Selection of materials as electrolytes
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/08—Selection of materials as electrolytes
- H01M10/10—Immobilising of electrolyte
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/12—Construction or manufacture
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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
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/42—Methods or arrangements for servicing or maintenance of secondary cells or secondary half-cells
- H01M2010/4292—Aspects relating to capacity ratio of electrodes/electrolyte or anode/cathode
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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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- 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
Definitions
- the present invention relates to a lead storage battery.
- the configuration using a mat separator as a lead-acid battery separator allows a sufficient amount of electrolyte to permeate the mat separator, so the amount of electrolyte used can be reduced compared to a configuration using a plate separator made of polyethylene or the like. Can be reduced. Therefore, the mat separator is an important element in a lead storage battery having a structure that does not perform rehydration such as a sealed lead storage battery. Recently, a configuration using a mat separator has also been adopted in lead storage batteries installed in automobiles, such as for auxiliary equipment of hybrid vehicles installed in places where it is difficult to supplement water.
- the above-described lead-acid battery for auxiliary machines plays a role of supplying electric power to various devices mounted on the vehicle even during a period when it is not charged for a long period of time (the vehicle is not driven), so that it easily falls into a relatively deep discharge.
- the discharge product (lead sulfate) and the active material (lead) of the negative electrode plate are easily dissolved in the electrolyte.
- a dendritic crystal of lead called dendrite is generated on the surface of the negative electrode plate and penetrates the mat separator to reach the positive electrode plate, thereby causing an internal short circuit (hereinafter referred to as this defect). This is called a dendrite short).
- Patent Document 1 discloses that the ratio S / P of the sulfuric acid mass S of the electrolytic solution to the mass P of the active material of the positive electrode plate is 0.40 or more and 0.52 or less. Discloses a technique for containing an appropriate amount of sodium tetraborate. Patent Document 2 discloses a technique for making the inner dimension of the cell chamber larger than the thickness of the electrode plate group while setting the above-described ratio S / P to 0.48 or more.
- the present invention is for solving this problem, and an object thereof is to provide a lead-acid battery capable of avoiding both problems such as a dendrite short circuit and a freezing breakage in a configuration in which the electrolyte is reduced using a mat separator. .
- a lead storage battery includes an electrode plate group, an electrolytic solution, and a battery case that accommodates them, and the electrode plate group includes a positive electrode plate, a negative electrode plate, And a ratio S / P of the sulfuric acid mass S to the active material mass P of the positive electrode plate is 0.53 or more, and the positive electrode plate and The thickness T of the side surface of the battery case parallel to the negative electrode plate is 3.5 mm or more and 5.5 mm or less.
- a lead-acid battery capable of avoiding both a dendrite short-circuit and a freezing breakage in a configuration in which the electrolyte is reduced using a mat separator.
- FIG. 1 is a diagram schematically showing a configuration of a lead storage battery according to an embodiment of the present invention.
- the lead storage battery includes an electrode plate group 1, an electrolytic solution (not shown), and a battery case 2 for storing them.
- the electrode plate group 1 includes a positive electrode plate 1a, a negative electrode plate 1b, and a mat separator 1c sandwiched between the two electrode plates.
- the plurality of electrode plate groups 1 are respectively stored in the cell chambers 2b of the battery case 2 partitioned by the middle partition plate 2a. And it connects with the different polarity of the adjacent electrode group 1 via the connection component 3 (series connection). Further, the opening of the battery case 2 is closed with a lid 4 having a control valve 4a corresponding to each cell chamber 2b. Instead of the control valve 4a, a simple liquid plug may be used.
- the lead storage battery of this embodiment has two features.
- the first characteristic is that the ratio S / P of the sulfuric acid mass S to the active material mass P of the positive electrode plate 1a is 0.53 or more.
- the second feature is that the thickness T of the side surface (hereinafter referred to as the short side surface 2c) of the battery case 2 parallel to the positive electrode plate 1a and the negative electrode plate 1b is 3.5 mm or more and 5.5 mm or less.
- Patent Document 1 states that when the ratio S / P exceeds 0.52, the gas absorption efficiency in the negative electrode plate 1b is lowered, gas generation becomes remarkable, and the reduction of the electrolyte becomes remarkable.
- the thickness of the short side surface 2c is 3.5 mm or more, the decrease in the electrolyte can be prevented.
- the inventors of the present invention have the reason that the sufficiently thick short side surface 2c presses the electrode plate group 1 so that the gap in the mat separator 1c, which serves as a passage for the generated gas, is narrowed, and the passing speed of the generated gas is reduced. It is presumed that the gas absorption efficiency has recovered due to the decrease (the generated gas slowly passes through the surface of the negative electrode plate 1b).
- the thickness of the short side surface 2c becomes excessively large and exceeds 5.5 mm, the gap in the separator 1c becomes too small (the mat separator 1c is compressed too much), and the positive electrode plate 1a and the negative electrode plate 1b. Too close, dendrite shorts are likely to occur.
- the ratio S / P is less than 5.3, the amount of sulfuric acid in the electrolyte solution becomes too low (too close to the additive-free water), so the freezing point of the electrolyte solution becomes high and used in cold regions. In this case, the electrolyte is more likely to freeze.
- the electrolytic solution whose volume is increased by freezing compresses the battery case 2 and causes the battery case 2 to freeze and break.
- the active material of the positive electrode plate 1a lead powder appropriately containing red lead or the like can be used.
- the active material of the negative electrode plate 1b can appropriately contain barium sulfate, a lignin compound, and the like in addition to the lead powder described above. Glass fiber or polyester fiber can be used as the main raw material for the mat separator 1c.
- the ratio S / P in the present invention is calculated from the active material mass P of the positive electrode plate 1a and the sulfuric acid mass S of the electrolyte solution for one electrode plate group 1, but for the entire lead acid battery, the positive electrode plate Even if it is calculated from the mass P of the active material 1a and the mass S of the sulfuric acid in the electrolyte, there is basically no significant difference.
- An active material paste is prepared by kneading lead oxide powder with sulfuric acid and purified water, and the active material paste is filled into a continuum of lattice obtained by expanding a lead alloy sheet, and cut into a predetermined size.
- a positive electrode plate 1a active material mass P was 80 g per sheet
- an active material paste is prepared by kneading a mixture of lead oxide powder with organic additives, barium sulfate, carbon, etc., using sulfuric acid and purified water, and then expanding the lead alloy sheet. The grid was filled with this active material paste to prepare a negative electrode plate 1b.
- An electrode plate group 1 was prepared by disposing a mat separator 1c mainly composed of glass fiber or polyester fiber between 5 positive electrode plates 1a and 6 negative electrode plates 1b.
- a plurality of electrode plate groups 1 were respectively stored in cell chambers 2b of a battery case 2 (thickness of the short side surface 2c is 4.5 mm), and different polarities of adjacent electrode plate groups 1 were connected by connecting parts 3.
- the positive electrode plate 1a of the cell chambers at both ends was connected to a positive terminal, and the negative electrode plate 1b was connected to a negative terminal.
- the opening of the battery case 2 is sealed with a lid 4, and dilute sulfuric acid that is an electrolytic solution (200 g of sulfuric acid, specific gravity is 1.33 g / ml) is injected from the liquid port. Sealed to produce a 12V28Ah lead acid battery (Battery A, ratio S / P is 0.5).
- the battery under each condition was charged at a constant voltage of 15.0 V (maximum current 25 A, 4 hours) in a 25 ° C. environment and discharged at 5.6 A for 4 hours. Thereafter, the reaction was allowed to stand for 24 hours in a ⁇ 40 ° C. environment, and further for 24 hours in a 5 ° C. environment, and was repeated 10 times. After that, the battery case 2 that was visually damaged was considered to have been frozen.
- the ratio S / P is less than 0.53, freezing damage is observed. This is because if the amount of sulfuric acid in the electrolytic solution becomes too low (too close to the additive-free water), the freezing point of the electrolytic solution becomes high, and the electrolytic solution whose volume is increased due to freezing of the electrolytic solution is This is probably because the battery case 2 was pressed and the battery case 2 was frozen. Therefore, it can be seen that the ratio S / P must be 0.53 or more.
- the electrolytic solution may overflow from the battery case 2. Therefore, in order to obtain the same ratio S / P without causing overflow of the electrolytic solution, the specific gravity of the electrolytic solution may be increased. However, if the specific gravity of the electrolytic solution is too large, the viscosity of the electrolytic solution becomes too high, which may reduce the high rate discharge characteristics of the battery, which is not preferable.
- the thickness of the short side surface 2c exceeds 5.5 mm, the short-circuit occurrence rate increases. This is because when the thickness of the short side surface 2c becomes excessively large, the gap in the separator 1c becomes too small (the mat separator 1c is compressed too much), and the positive electrode plate 1a and the negative electrode plate 1b approach too much. This is probably because dendrite shorts are more likely to occur. Therefore, it can be seen that the thickness of the short side surface 2c must be not less than 3.5 mm and not more than 5.5 mm.
- Embodiment 1 and Examples a plurality of electrode plate groups 1 are provided and adjacent electrode plate groups 1 are connected in series. However, even when a plurality of electrode plate groups 1 are connected in parallel, the electrode plates Even when only one group 1 is used, the same effect can be obtained.
- the lead storage battery that can obtain the above-described effect usually has an electrolyte solution in which at least a part of the electrode plate group 1 is usually immersed, although depending on the pore volume of the mat separator 1c and the like.
- the lead storage battery of the present invention can improve both the balance including other characteristics while avoiding both problems such as dendrite short-circuit and freezing breakage in a configuration in which the electrolyte is reduced by using a mat separator. Therefore, it is extremely useful industrially, such as development of hybrid vehicles for auxiliary machines.
- Electrode plate group 1a Positive electrode plate 1b Negative electrode plate 1c Mat separator 2 Battery case 2a Middle partition plate 2b Cell chamber 2c Short side surface 3 Connection component 4 Lid 4a Control valve
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Abstract
The present invention provides a lead-acid cell capable of avoiding both the problems of dendrite short circuits and freeze damage in a configuration in which a mat separator is used and the amount of electrolyte is reduced. This lead-acid cell is provided with an electrode plate group (1), an electrolyte, and a cell case (2) for housing the electrode plate group (1) and the electrolyte. The electrode plate group (1) comprises a positive electrode plate (1a), a negative electrode plate (1b), and a mat separator (1c) flanked by the two electrode plates. The ratio (S/P) of the mass (S) of the sulfuric acid in the electrolyte relative to the mass (P) of the active material of the positive electrode plate (1a) is equal to or greater than 0.53. The thickness (T) of the side surface of the cell case (2) parallel to the positive electrode plate (1a) and the negative electrode plate (1b) is 3.5-5.5 mm.
Description
本発明は、鉛蓄電池に関する。
The present invention relates to a lead storage battery.
鉛蓄電池のセパレータとしてマットセパレータを用いた構成は、十分な電解液をマットセパレータに浸透させることができるので、ポリエチレンなどからなる板状のセパレータを用いた構成に比べて、電解液の使用量を減らすことができる。したがってマットセパレータは、密閉式鉛蓄電池など補水を行わない構成の鉛蓄電池において重要な要素となる。最近では、補水を行い難い箇所に設置されるハイブリッド車両の補機用など、自動車に搭載される鉛蓄電池にも、マットセパレータを用いた構成が採用されるようになった。
The configuration using a mat separator as a lead-acid battery separator allows a sufficient amount of electrolyte to permeate the mat separator, so the amount of electrolyte used can be reduced compared to a configuration using a plate separator made of polyethylene or the like. Can be reduced. Therefore, the mat separator is an important element in a lead storage battery having a structure that does not perform rehydration such as a sealed lead storage battery. Recently, a configuration using a mat separator has also been adopted in lead storage batteries installed in automobiles, such as for auxiliary equipment of hybrid vehicles installed in places where it is difficult to supplement water.
上述した補機用の鉛蓄電池は、長期間充電されない(車が運転されない)期間にも、車載された様々な機器に電力を供給する役割を担うので、比較的深い放電に陥りやすい。深い放電に陥った鉛蓄電池の内部では、放電生成物(硫酸鉛)や負極板の活物質(鉛)が電解液に溶解しやすくなる。この状態から充電を開始すると、負極板の表面でデンドライトと呼ばれる鉛の樹枝状結晶が生成し、マットセパレータを貫通して正極板に到達することで、内部短絡が発生する(以下、この不具合をデンドライトショートと称する)。
The above-described lead-acid battery for auxiliary machines plays a role of supplying electric power to various devices mounted on the vehicle even during a period when it is not charged for a long period of time (the vehicle is not driven), so that it easily falls into a relatively deep discharge. Inside the lead-acid battery that is deeply discharged, the discharge product (lead sulfate) and the active material (lead) of the negative electrode plate are easily dissolved in the electrolyte. When charging is started from this state, a dendritic crystal of lead called dendrite is generated on the surface of the negative electrode plate and penetrates the mat separator to reach the positive electrode plate, thereby causing an internal short circuit (hereinafter referred to as this defect). This is called a dendrite short).
このような不具合を解消するため、特許文献1には、正極板の活物質の質量Pに対する電解液の硫酸の質量Sの比S/Pを0.40以上0.52以下にしつつ、電解液に四硼酸ナトリウムを適量含ませる技術が開示されている。また、特許文献2には、上述した比S/Pを0.48以上にしつつ、セル室の内寸を極板群の厚みよりも大きくする技術が開示されている。
In order to eliminate such problems, Patent Document 1 discloses that the ratio S / P of the sulfuric acid mass S of the electrolytic solution to the mass P of the active material of the positive electrode plate is 0.40 or more and 0.52 or less. Discloses a technique for containing an appropriate amount of sodium tetraborate. Patent Document 2 discloses a technique for making the inner dimension of the cell chamber larger than the thickness of the electrode plate group while setting the above-described ratio S / P to 0.48 or more.
近年、ハイブリッド車両などが寒冷地で用いられることが増える中、マットセパレータを用いた車載用の鉛蓄電池の電槽が破損する不具合(以下、この不具合を凍結破損と称する)が懸念され始めた。そして特許文献1や2の技術だけでは、凍結破損を十分に回避できないことがわかってきた。
In recent years, as hybrid vehicles and the like have been used in cold regions, there has been a concern about the failure (hereinafter referred to as “freezing failure”) of the battery case of the lead-acid battery for vehicles using a mat separator. And it has been found that freezing breakage cannot be sufficiently avoided only by the techniques of Patent Documents 1 and 2.
本発明はこの課題を解決するためのものであって、マットセパレータを用いて電解液を少なくした構成において、デンドライトショートと凍結破損という不具合の双方を回避できる鉛蓄電池を提供することを目的とする。
The present invention is for solving this problem, and an object thereof is to provide a lead-acid battery capable of avoiding both problems such as a dendrite short circuit and a freezing breakage in a configuration in which the electrolyte is reduced using a mat separator. .
前述した課題を解決するために、本発明に係る鉛蓄電池は、極板群と、電解液と、これらを収納する電槽とを備え、極板群は、正極板と、負極板と、この2つの極板に挟まれたマットセパレータとで構成されており、正極板の活物質の質量Pに対する電解液の硫酸の質量Sの比S/Pが、0.53以上であり、正極板および負極板に平行な電槽の側面の厚みTが、3.5mm以上5.5mm以下であることを特徴とする。
In order to solve the above-described problems, a lead storage battery according to the present invention includes an electrode plate group, an electrolytic solution, and a battery case that accommodates them, and the electrode plate group includes a positive electrode plate, a negative electrode plate, And a ratio S / P of the sulfuric acid mass S to the active material mass P of the positive electrode plate is 0.53 or more, and the positive electrode plate and The thickness T of the side surface of the battery case parallel to the negative electrode plate is 3.5 mm or more and 5.5 mm or less.
本発明を用いれば、マットセパレータを用いて電解液を少なくした構成において、デンドライトショートと凍結破損という不具合の双方を回避できる鉛蓄電池を提供することができる。
According to the present invention, it is possible to provide a lead-acid battery capable of avoiding both a dendrite short-circuit and a freezing breakage in a configuration in which the electrolyte is reduced using a mat separator.
以下、本発明の実施の形態を、図を用いて説明する。
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
図1は、本発明の一実施形態における鉛蓄電池の構成を模式的に示した図である。
FIG. 1 is a diagram schematically showing a configuration of a lead storage battery according to an embodiment of the present invention.
鉛蓄電池は、極板群1と、電解液(図示せず)と、これらを収納する電槽2とを備える。極板群1は、正極板1aと、負極板1bと、この2つの極板に挟まれたマットセパレータ1cとで構成されている。複数の極板群1は、中仕切板2aで区切られた電槽2のセル室2bにそれぞれ収納される。そして、接続部品3を介して、隣り合う極板群1の異なる極性と接続される(直列接続)。さらに、電槽2の開口部を、各々のセル室2bに対応する制御弁4aを有する蓋4で閉じる。なお、制御弁4aの代わりに、単なる液口栓を用いても良い。
The lead storage battery includes an electrode plate group 1, an electrolytic solution (not shown), and a battery case 2 for storing them. The electrode plate group 1 includes a positive electrode plate 1a, a negative electrode plate 1b, and a mat separator 1c sandwiched between the two electrode plates. The plurality of electrode plate groups 1 are respectively stored in the cell chambers 2b of the battery case 2 partitioned by the middle partition plate 2a. And it connects with the different polarity of the adjacent electrode group 1 via the connection component 3 (series connection). Further, the opening of the battery case 2 is closed with a lid 4 having a control valve 4a corresponding to each cell chamber 2b. Instead of the control valve 4a, a simple liquid plug may be used.
本実施形態の鉛蓄電池は、2つの特徴を有する。正極板1aの活物質の質量Pに対する電解液の硫酸の質量Sの比S/Pが0.53以上であることが、第1の特徴である。正極板1aおよび負極板1bに平行な電槽2の側面(以下、短側面2cと称する)の厚みTが3.5mm以上5.5mm以下であることが、第2の特徴である。
The lead storage battery of this embodiment has two features. The first characteristic is that the ratio S / P of the sulfuric acid mass S to the active material mass P of the positive electrode plate 1a is 0.53 or more. The second feature is that the thickness T of the side surface (hereinafter referred to as the short side surface 2c) of the battery case 2 parallel to the positive electrode plate 1a and the negative electrode plate 1b is 3.5 mm or more and 5.5 mm or less.
特許文献1には、比S/Pが0.52を超えると、負極板1bでのガス吸収効率が低下してガス発生が顕著化し、電解液の減少が著しくなると記されている。ところが本発明者らが鋭意検討した結果、短側面2cの厚みを3.5mm以上にすれば、電解液の減少を防げることを知見するに至った。本発明者らは、この理由を、十分に厚い短側面2cが極板群1を押圧することで、発生したガスの抜け道となるマットセパレータ1c中の間隙が細くなり、発生ガスの通過速度が低下する(発生ガスが負極板1bの表面をゆっくりと通過するようになる)ことで、ガス吸収効率が持ち直したからであると推測している。
Patent Document 1 states that when the ratio S / P exceeds 0.52, the gas absorption efficiency in the negative electrode plate 1b is lowered, gas generation becomes remarkable, and the reduction of the electrolyte becomes remarkable. However, as a result of intensive studies by the present inventors, it has been found that if the thickness of the short side surface 2c is 3.5 mm or more, the decrease in the electrolyte can be prevented. The inventors of the present invention have the reason that the sufficiently thick short side surface 2c presses the electrode plate group 1 so that the gap in the mat separator 1c, which serves as a passage for the generated gas, is narrowed, and the passing speed of the generated gas is reduced. It is presumed that the gas absorption efficiency has recovered due to the decrease (the generated gas slowly passes through the surface of the negative electrode plate 1b).
しかしながら、短側面2cの厚みが過度に大きくなって、5.5mmを超えると、セパレータ1c中の間隙が少なくなりすぎて(マットセパレータ1cが押し縮められすぎて)、正極板1aと負極板1bとが過度に近づくことで、デンドライトショートが起こりやすくなる。
However, if the thickness of the short side surface 2c becomes excessively large and exceeds 5.5 mm, the gap in the separator 1c becomes too small (the mat separator 1c is compressed too much), and the positive electrode plate 1a and the negative electrode plate 1b. Too close, dendrite shorts are likely to occur.
一方で、比S/Pが5.3を下回ると、電解液に占める硫酸の量が低くなりすぎる(無添加の水に近づきすぎる)ので、電解液の凝固点が高くなり、寒冷地で使用した際に電解液が凍りやすくなる。凍ることで体積を増した電解液は電槽2を圧迫し、電槽2の凍結破損を起こす。
On the other hand, when the ratio S / P is less than 5.3, the amount of sulfuric acid in the electrolyte solution becomes too low (too close to the additive-free water), so the freezing point of the electrolyte solution becomes high and used in cold regions. In this case, the electrolyte is more likely to freeze. The electrolytic solution whose volume is increased by freezing compresses the battery case 2 and causes the battery case 2 to freeze and break.
正極板1aの活物質には、鉛丹などを適宜含む鉛粉を用いることができる。負極板1bの活物質には、上述した鉛粉の他に、硫酸バリウムやリグニン化合物などを適宜含ませることができる。マットセパレータ1cには、ガラス繊維やポリエステル繊維を主原材料として用いることができる。
As the active material of the positive electrode plate 1a, lead powder appropriately containing red lead or the like can be used. The active material of the negative electrode plate 1b can appropriately contain barium sulfate, a lignin compound, and the like in addition to the lead powder described above. Glass fiber or polyester fiber can be used as the main raw material for the mat separator 1c.
なお、本発明における比S/Pは、1つの極板群1について、正極板1aの活物質の質量Pと電解液の硫酸の質量Sとから算出されるが、鉛蓄電池全体について、正極板1aの活物質の質量Pと電解液の硫酸の質量Sとから算出しても、基本的に大差がない。
The ratio S / P in the present invention is calculated from the active material mass P of the positive electrode plate 1a and the sulfuric acid mass S of the electrolyte solution for one electrode plate group 1, but for the entire lead acid battery, the positive electrode plate Even if it is calculated from the mass P of the active material 1a and the mass S of the sulfuric acid in the electrolyte, there is basically no significant difference.
以下、実施例により、本発明の効果を説明する。
Hereinafter, the effect of the present invention will be described with reference to examples.
(電池A)
酸化鉛粉を硫酸と精製水とで混練して活物質ペーストを作製し、鉛合金シートをエキスパンド展開して得た格子の連続体にこの活物質ペーストを充填し、所定の寸法に切断して正極板1a(活物質の質量Pが1枚当たり80g)を作製した。一方、酸化鉛粉に対して有機添加剤や硫酸バリウム、カーボンなどを常法により添加したものを硫酸と精製水とで混練して活物質ペーストを作製し、鉛合金シートをエキスパンド展開して得た格子にこの活物質ペーストを充填し、負極板1bを作製した。 (Battery A)
An active material paste is prepared by kneading lead oxide powder with sulfuric acid and purified water, and the active material paste is filled into a continuum of lattice obtained by expanding a lead alloy sheet, and cut into a predetermined size. Apositive electrode plate 1a (active material mass P was 80 g per sheet) was produced. On the other hand, an active material paste is prepared by kneading a mixture of lead oxide powder with organic additives, barium sulfate, carbon, etc., using sulfuric acid and purified water, and then expanding the lead alloy sheet. The grid was filled with this active material paste to prepare a negative electrode plate 1b.
酸化鉛粉を硫酸と精製水とで混練して活物質ペーストを作製し、鉛合金シートをエキスパンド展開して得た格子の連続体にこの活物質ペーストを充填し、所定の寸法に切断して正極板1a(活物質の質量Pが1枚当たり80g)を作製した。一方、酸化鉛粉に対して有機添加剤や硫酸バリウム、カーボンなどを常法により添加したものを硫酸と精製水とで混練して活物質ペーストを作製し、鉛合金シートをエキスパンド展開して得た格子にこの活物質ペーストを充填し、負極板1bを作製した。 (Battery A)
An active material paste is prepared by kneading lead oxide powder with sulfuric acid and purified water, and the active material paste is filled into a continuum of lattice obtained by expanding a lead alloy sheet, and cut into a predetermined size. A
この正極板1a5枚と負極板1b6枚との間にガラス繊維やポリエステル繊維を主成分とするマットセパレータ1cをそれぞれ配置することにより、極板群1を作製した。
An electrode plate group 1 was prepared by disposing a mat separator 1c mainly composed of glass fiber or polyester fiber between 5 positive electrode plates 1a and 6 negative electrode plates 1b.
複数の極板群1を、電槽2(短側面2cの厚みが4.5mm)のセル室2bにそれぞれ収納し、隣り合った極板群1の異なる極性どうしを接続部品3で接続した。両端のセル室の正極板1aは正極性の端子に、負極板1bは負極性の端子にそれぞれ接続した。電槽2の開口部を蓋4で封止して、液口から電解液である希硫酸(硫酸の質量が200g、比重が1.33g/ml)を注入し、液口を制御弁4aで封止して、12V28Ahの鉛蓄電池(電池A、比S/Pが0.5)を作製した。
A plurality of electrode plate groups 1 were respectively stored in cell chambers 2b of a battery case 2 (thickness of the short side surface 2c is 4.5 mm), and different polarities of adjacent electrode plate groups 1 were connected by connecting parts 3. The positive electrode plate 1a of the cell chambers at both ends was connected to a positive terminal, and the negative electrode plate 1b was connected to a negative terminal. The opening of the battery case 2 is sealed with a lid 4, and dilute sulfuric acid that is an electrolytic solution (200 g of sulfuric acid, specific gravity is 1.33 g / ml) is injected from the liquid port. Sealed to produce a 12V28Ah lead acid battery (Battery A, ratio S / P is 0.5).
(電池B、C、D、E、F)
電池Aよりも希硫酸の容積を増やす(硫酸の質量Sを大きくする)ことで、比S/Pを(表1)に示すように電池Aよりも大きくしたこと以外、電池Aと同じ方法で電池B、C、D、E、およびFを作製した。 (Batteries B, C, D, E, F)
By increasing the volume of dilute sulfuric acid compared to battery A (increasing the mass S of sulfuric acid), the ratio S / P was made larger than that of battery A as shown in (Table 1). Batteries B, C, D, E, and F were made.
電池Aよりも希硫酸の容積を増やす(硫酸の質量Sを大きくする)ことで、比S/Pを(表1)に示すように電池Aよりも大きくしたこと以外、電池Aと同じ方法で電池B、C、D、E、およびFを作製した。 (Batteries B, C, D, E, F)
By increasing the volume of dilute sulfuric acid compared to battery A (increasing the mass S of sulfuric acid), the ratio S / P was made larger than that of battery A as shown in (Table 1). Batteries B, C, D, E, and F were made.
(電池I、J、K、L、M、N)
(表1)に示すように、電池Dよりも電槽2の短側面2cを薄くしたり(電池I、J、K)厚くしたり(電池L、M、N)したこと以外、電池Dと同じ方法で電池I、J、K、L、MおよびNを作製した。 (Batteries I, J, K, L, M, N)
As shown in (Table 1), except that theshort side surface 2c of the battery case 2 is thinner (batteries I, J, K) than the battery D (batteries L, M, N), and the battery D Batteries I, J, K, L, M and N were made in the same manner.
(表1)に示すように、電池Dよりも電槽2の短側面2cを薄くしたり(電池I、J、K)厚くしたり(電池L、M、N)したこと以外、電池Dと同じ方法で電池I、J、K、L、MおよびNを作製した。 (Batteries I, J, K, L, M, N)
As shown in (Table 1), except that the
これらの電池について以下の評価を行った。結果を(表1)に併記する。
These batteries were evaluated as follows. The results are also shown in (Table 1).
(デンドライトショート)
各条件の電池それぞれ10個に対し、40℃環境下で、5.6Aで10.5Vまで放電(いわゆる完全放電)を行った後、10Wの負荷を付けて14日過放電を行った。次いで、40℃環境下で、開路状態で14日放置した。最後に25℃環境下で、15.0V定電圧充電(最大電流25A、4時間)を行った後、各条件の電池を分解した。マットセパレータ1cの正極板1aと接する側に黒点(デンドライト)が1つでも観測されれば短絡(デンドライトショート)が発生したものとみなした。 (Dendrite short)
10 batteries under each condition were discharged to 10.5 V at 5.6 A in a 40 ° C. environment (so-called complete discharge), and then overdischarged for 14 days with a load of 10 W. Next, it was left in an open circuit state for 14 days in a 40 ° C. environment. Finally, 15.0 V constant voltage charging (maximum current 25 A, 4 hours) was performed in a 25 ° C. environment, and then the battery under each condition was disassembled. If even one black spot (dendrite) is observed on the side of the mat separator 1c that contacts the positive electrode plate 1a, it is considered that a short circuit (dendrite short) has occurred.
各条件の電池それぞれ10個に対し、40℃環境下で、5.6Aで10.5Vまで放電(いわゆる完全放電)を行った後、10Wの負荷を付けて14日過放電を行った。次いで、40℃環境下で、開路状態で14日放置した。最後に25℃環境下で、15.0V定電圧充電(最大電流25A、4時間)を行った後、各条件の電池を分解した。マットセパレータ1cの正極板1aと接する側に黒点(デンドライト)が1つでも観測されれば短絡(デンドライトショート)が発生したものとみなした。 (Dendrite short)
10 batteries under each condition were discharged to 10.5 V at 5.6 A in a 40 ° C. environment (so-called complete discharge), and then overdischarged for 14 days with a load of 10 W. Next, it was left in an open circuit state for 14 days in a 40 ° C. environment. Finally, 15.0 V constant voltage charging (
(凍結破損)
各条件の電池に対し、25℃環境下で15.0V定電圧充電(最大電流25A、4時間)を行い、5.6Aで4時間放電した。その後、-40℃環境下で24時間放置し、さらに、5℃環境下で24時間放置することを10回繰り返した。その後に電槽2の破損が目視できたものは、凍結破損があったものとみなした。 (Freezing damage)
The battery under each condition was charged at a constant voltage of 15.0 V (maximum current 25 A, 4 hours) in a 25 ° C. environment and discharged at 5.6 A for 4 hours. Thereafter, the reaction was allowed to stand for 24 hours in a −40 ° C. environment, and further for 24 hours in a 5 ° C. environment, and was repeated 10 times. After that, thebattery case 2 that was visually damaged was considered to have been frozen.
各条件の電池に対し、25℃環境下で15.0V定電圧充電(最大電流25A、4時間)を行い、5.6Aで4時間放電した。その後、-40℃環境下で24時間放置し、さらに、5℃環境下で24時間放置することを10回繰り返した。その後に電槽2の破損が目視できたものは、凍結破損があったものとみなした。 (Freezing damage)
The battery under each condition was charged at a constant voltage of 15.0 V (maximum current 25 A, 4 hours) in a 25 ° C. environment and discharged at 5.6 A for 4 hours. Thereafter, the reaction was allowed to stand for 24 hours in a −40 ° C. environment, and further for 24 hours in a 5 ° C. environment, and was repeated 10 times. After that, the
(電解液の減少)
各条件の電池に対し、40℃環境下で、14.4Vの定電圧充電を、28日間に亘って行った。電池の初期重量と試験後の重量との差を電解液の減少量とみなし、この値を電池の初期重量で除することで電解液の減少率を求めた。 (Reduction of electrolyte)
The battery under each condition was charged with a constant voltage of 14.4 V for 28 days in a 40 ° C. environment. The difference between the initial weight of the battery and the weight after the test was regarded as a decrease amount of the electrolytic solution, and this value was divided by the initial weight of the battery to obtain the decreasing rate of the electrolytic solution.
各条件の電池に対し、40℃環境下で、14.4Vの定電圧充電を、28日間に亘って行った。電池の初期重量と試験後の重量との差を電解液の減少量とみなし、この値を電池の初期重量で除することで電解液の減少率を求めた。 (Reduction of electrolyte)
The battery under each condition was charged with a constant voltage of 14.4 V for 28 days in a 40 ° C. environment. The difference between the initial weight of the battery and the weight after the test was regarded as a decrease amount of the electrolytic solution, and this value was divided by the initial weight of the battery to obtain the decreasing rate of the electrolytic solution.
電池A~Gを対比する。比S/Pが0.53を下回ると、凍結破損が見られる。これは、電解液に占める硫酸の量が低くなりすぎる(無添加の水に近づきすぎる)と、電解液の凝固点が高くなり、電解液が凍ることで体積を増した電解液が電槽2を圧迫し、電槽2の凍結破損に至ったためと考えられる。よって、比S/Pは0.53以上でなければならないことがわかる。
Contrast batteries A to G. When the ratio S / P is less than 0.53, freezing damage is observed. This is because if the amount of sulfuric acid in the electrolytic solution becomes too low (too close to the additive-free water), the freezing point of the electrolytic solution becomes high, and the electrolytic solution whose volume is increased due to freezing of the electrolytic solution is This is probably because the battery case 2 was pressed and the battery case 2 was frozen. Therefore, it can be seen that the ratio S / P must be 0.53 or more.
なお、希硫酸の容積を増す(硫酸の質量Sを大きくする)ことによって、比S/Pを大きくすると、電解液が電槽2から溢れてしまうおそれがある。そこで、電解液の溢れが生じないようにして、同じ大きさの比S/Pを得るには、電解液の比重を大きくすればよい。しかしながら、電解液の比重を大きくしすぎると、電解液の粘度が高くなりすぎ、これにより、電池の高率放電特性が低下するおそれがあり、あまり好ましくない。
If the ratio S / P is increased by increasing the volume of dilute sulfuric acid (increasing the mass S of sulfuric acid), the electrolytic solution may overflow from the battery case 2. Therefore, in order to obtain the same ratio S / P without causing overflow of the electrolytic solution, the specific gravity of the electrolytic solution may be increased. However, if the specific gravity of the electrolytic solution is too large, the viscosity of the electrolytic solution becomes too high, which may reduce the high rate discharge characteristics of the battery, which is not preferable.
電池Dと電池I~Nとを比較する。電槽2の短側面2cの厚みが3.5mm以上になると、電解液の減少が著しく低下する。これは、十分に厚い短側面2cが極板群1を押圧することで、発生したガスの抜け道となるマットセパレータ1c中の間隙が細くなり、発生ガスの通過速度が低下する(発生ガスが負極板1bの表面をゆっくりと通過するようになる)ことによって、ガス吸収効率が持ち直したためと考えられる。
Compare battery D and batteries I-N. When the thickness of the short side surface 2c of the battery case 2 is 3.5 mm or more, the decrease in the electrolytic solution is remarkably reduced. This is because when the sufficiently thick short side surface 2c presses the electrode plate group 1, the gap in the mat separator 1c, which serves as a passage for the generated gas, is narrowed, and the passing speed of the generated gas is reduced (the generated gas is a negative electrode). It is considered that the gas absorption efficiency has been recovered by slowly passing through the surface of the plate 1b.
一方で、短側面2cの厚みが5.5mmを超えると、短絡発生率が高くなる。これは、短側面2cの厚みが過度に大きくなると、セパレータ1c中の間隙が少なくなりすぎて(マットセパレータ1cが押し縮められすぎて)、正極板1aと負極板1bとが過度に近づくため、デンドライトショートが起こりやすくなったためと考えられる。よって、短側面2cの厚みは3.5mm以上5.5mm以下でなければいけないことがわかる。
On the other hand, when the thickness of the short side surface 2c exceeds 5.5 mm, the short-circuit occurrence rate increases. This is because when the thickness of the short side surface 2c becomes excessively large, the gap in the separator 1c becomes too small (the mat separator 1c is compressed too much), and the positive electrode plate 1a and the negative electrode plate 1b approach too much. This is probably because dendrite shorts are more likely to occur. Therefore, it can be seen that the thickness of the short side surface 2c must be not less than 3.5 mm and not more than 5.5 mm.
なお実施形態1および実施例では、極板群1を複数備え、隣り合う極板群1を直列に接続した態様を示したが、複数の極板群1を並列に接続した場合でも、極板群1を1つのみ用いた場合でも、同様の効果が得られる。
In Embodiment 1 and Examples, a plurality of electrode plate groups 1 are provided and adjacent electrode plate groups 1 are connected in series. However, even when a plurality of electrode plate groups 1 are connected in parallel, the electrode plates Even when only one group 1 is used, the same effect can be obtained.
また上述した効果が得られる鉛蓄電池は、マットセパレータ1cなどが有する空孔体積の大小にもよるが、通常は電解液が極板群1の少なくとも一部を浸漬している場合が多い。
In addition, the lead storage battery that can obtain the above-described effect usually has an electrolyte solution in which at least a part of the electrode plate group 1 is usually immersed, although depending on the pore volume of the mat separator 1c and the like.
本発明の鉛蓄電池は、マットセパレータを用いて電解液を少なくした構成において、デンドライトショートと凍結破損という不具合の双方を回避しつつ、他の特性を含めたバランスも高めることができる。よってハイブリッド車両の補機用への展開など、工業上、極めて有用である。
The lead storage battery of the present invention can improve both the balance including other characteristics while avoiding both problems such as dendrite short-circuit and freezing breakage in a configuration in which the electrolyte is reduced by using a mat separator. Therefore, it is extremely useful industrially, such as development of hybrid vehicles for auxiliary machines.
1 極板群
1a 正極板
1b 負極板
1c マットセパレータ
2 電槽
2a 中仕切板
2b セル室
2c 短側面
3 接続部品
4 蓋
4a 制御弁 DESCRIPTION OFSYMBOLS 1 Electrode plate group 1a Positive electrode plate 1b Negative electrode plate 1c Mat separator 2 Battery case 2a Middle partition plate 2b Cell chamber 2c Short side surface 3 Connection component 4 Lid 4a Control valve
1a 正極板
1b 負極板
1c マットセパレータ
2 電槽
2a 中仕切板
2b セル室
2c 短側面
3 接続部品
4 蓋
4a 制御弁 DESCRIPTION OF
Claims (4)
- 極板群と、電解液と、これらを収納する電槽とを備え、
前記極板群は、正極板と、負極板と、この2つの極板に挟まれたマットセパレータとで構成されており、
前記正極板の活物質の質量Pに対する前記電解液の硫酸の質量Sの比S/Pが、0.53以上であり、
前記正極板および前記負極板に平行な前記電槽の側面の厚みTが、3.5mm以上5.5mm以下である鉛蓄電池。 An electrode plate group, an electrolytic solution, and a battery case for storing them,
The electrode plate group includes a positive electrode plate, a negative electrode plate, and a mat separator sandwiched between the two electrode plates,
A ratio S / P of a mass S of sulfuric acid in the electrolytic solution to a mass P of the active material of the positive electrode plate is 0.53 or more,
A lead acid battery in which a thickness T of a side surface of the battery case parallel to the positive electrode plate and the negative electrode plate is 3.5 mm or more and 5.5 mm or less. - 前記正極板の活物質の質量Pに対する前記電解液の硫酸の質量Sの比S/Pが、0.67以下でありことを特徴とする、請求項1に記載の鉛蓄電池。 2. The lead acid battery according to claim 1, wherein a ratio S / P of a mass S of sulfuric acid of the electrolytic solution to a mass P of the active material of the positive electrode plate is 0.67 or less.
- 前記極板群を複数備え、隣り合う前記極板群を直列に接続したことを特徴とする、請求項1に記載の鉛蓄電池。 The lead acid battery according to claim 1, wherein a plurality of the electrode plate groups are provided, and the adjacent electrode plate groups are connected in series.
- 前記電解液が前記極板群の少なくとも一部を浸漬していることを特徴とする、請求項1に記載の鉛蓄電池。 The lead acid battery according to claim 1, wherein the electrolytic solution immerses at least a part of the electrode plate group.
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2013
- 2013-10-21 JP JP2013556443A patent/JPWO2014076883A1/en active Pending
- 2013-10-21 WO PCT/JP2013/006224 patent/WO2014076883A1/en active Application Filing
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JPS62119875A (en) * | 1985-11-18 | 1987-06-01 | Yuasa Battery Co Ltd | Lead storage battery |
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