WO2019225389A1 - Lead storage battery - Google Patents
Lead storage battery Download PDFInfo
- Publication number
- WO2019225389A1 WO2019225389A1 PCT/JP2019/019021 JP2019019021W WO2019225389A1 WO 2019225389 A1 WO2019225389 A1 WO 2019225389A1 JP 2019019021 W JP2019019021 W JP 2019019021W WO 2019225389 A1 WO2019225389 A1 WO 2019225389A1
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- WO
- WIPO (PCT)
- Prior art keywords
- electrode plate
- positive electrode
- perforated sheet
- negative electrode
- storage 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.)
- Ceased
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/463—Separators, membranes or diaphragms characterised by their shape
- H01M50/466—U-shaped, bag-shaped or folded
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/409—Separators, membranes or diaphragms characterised by the material
- H01M50/449—Separators, membranes or diaphragms characterised by the material having a layered structure
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/471—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof
- H01M50/474—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof characterised by their position inside the cells
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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
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/471—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof
- H01M50/477—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof characterised by their shape
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M50/00—Constructional details or processes of manufacture of the non-active parts of electrochemical cells other than fuel cells, e.g. hybrid cells
- H01M50/40—Separators; Membranes; Diaphragms; Spacing elements inside cells
- H01M50/471—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof
- H01M50/48—Spacing elements inside cells other than separators, membranes or diaphragms; Manufacturing processes thereof characterised by the material
- H01M50/483—Inorganic material
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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.
- a positive electrode plate, a negative electrode plate, a separator disposed between the positive electrode plate and the negative electrode plate, an electrolytic solution, and a battery case that accommodates the positive electrode plate, the negative electrode plate, the separator, and the electrolytic solution are provided.
- a lead storage battery is known (for example, Patent Document 1).
- a film body is attached to the surface of the negative electrode plate.
- the film body includes a base material and a hydrophilic film that covers the surface of the base material.
- the upper part of the negative electrode plate is higher than the lower part of the negative electrode plate.
- This embodiment makes it a subject to provide the lead storage battery with which durability with respect to repeated charging / discharging was improved.
- the lead storage battery of the present embodiment includes a positive electrode plate, a negative electrode plate, a perforated sheet disposed between the positive electrode plate and the negative electrode plate and having a through-hole formed in the thickness direction, and an electrolyte solution.
- the aperture ratio is different between the upper part and the lower part.
- FIG. 1 is a view showing an appearance and a part of the inside of the lead storage battery according to the present embodiment.
- FIG. 2 is a partial cross-sectional view of the electrode plate group in the lead storage battery according to the present embodiment.
- FIG. 3 is a schematic view of an example of a perforated sheet viewed from one side in the thickness direction.
- FIG. 4 is a graph showing the relationship between the discharge time and the electrode plate potential difference in a lead storage battery.
- each component (each component) of this embodiment is a thing in this embodiment, and may differ from the name of each component (each component) in background art.
- the lead storage battery 1 of the present embodiment is a lead storage battery that includes an aqueous sulfuric acid solution as an electrolyte, has lead dioxide or lead sulfate as an active material for the positive electrode, and has metallic lead or lead sulfate as the active material for the negative electrode.
- the lead storage battery 1 supplies electric energy to the outside during discharging and stores the electric energy inside during charging.
- the lead-acid battery 1 includes a battery case 60 (case), an electrolytic solution housed in the battery case 60 (case), and a plurality of electrode plate groups 10 immersed in the electrolytic solution. ,including.
- the lead acid battery 1 further includes a positive electrode terminal 70, a negative electrode terminal 80, and a connection member 90 that electrically connects the plurality of electrode plate groups 10 in series.
- the lead storage battery 1 supplies the electrical energy stored in the plurality of electrode plate groups 10 to the outside via the positive electrode terminal 70 and the negative electrode terminal 80, or stores the electric energy from the outside in the plurality of electrode plate groups 10. Is configured to do.
- the lead storage battery 1 of this embodiment is a liquid lead storage battery.
- the battery case 60 (case) has a rectangular parallelepiped shape having a rectangular bottom surface.
- the battery case 60 (case) includes a case main body 61 that opens upward, and a lid portion 62 that closes the opening of the case main body 61.
- the case main body 61 has a plurality of cell chambers formed by partitioning the internal space by partition walls. The plurality of cell chambers are arranged in the same direction (horizontal direction) as the long side direction of the bottom surface. Each cell chamber accommodates an electrolytic solution and one electrode plate group 10.
- the lid 62 has a liquid port plug 91 that can discharge the gas generated inside the battery to the outside of the battery.
- Each electrode plate group 10 includes a plurality of positive plates 20 (positive electrodes), a plurality of negative plates 30 (negative electrodes), a plurality of separators 40 for physically separating the positive plates 20 and the negative plates 30, and positive plates.
- 20 includes a positive electrode strap 71 that electrically connects the two electrodes 20 in parallel and a negative electrode strap 81 that electrically connects the negative electrode plates 30 in parallel.
- each electrode plate group 10 further includes a perforated sheet 50 disposed between the positive electrode plate 20 and the negative electrode plate 30 and having a through hole A formed in the thickness direction.
- a plurality of positive electrodes 20, a plurality of separators 40, and a plurality of negative electrodes 30 are stacked in the thickness direction.
- the thickness direction (stacking direction) of the positive electrode plate 20 and the negative electrode plate 30 of each electrode plate group 10 is the same as the direction in which the plurality of electrode plate groups 10 are arranged in the battery case 60 (case).
- the separator 40 is disposed between the positive electrode plate 20 and the negative electrode plate 30.
- the positive electrode strap 71 of one electrode plate group 10 and the negative electrode strap 81 of the other electrode plate group 10 are connected by the connection member 90.
- the plurality of electrode plate groups 10 are electrically connected in series.
- the perforated sheet 50 is disposed between the positive electrode plate 20 and the separator 40 or between the negative electrode plate 30 and the separator 40.
- the perforated sheet 50 is formed of a porous base material impregnated with an electrolytic solution.
- the perforated sheet 50 is formed with a plurality of through holes A penetrating in the thickness direction.
- the thickness of the portion of the separator 40 where the through hole A is not formed may be 0.01 mm or more and 2.0 mm or less in a state where the separator 40 is not compressed in the thickness direction.
- the “through hole” means a hole penetrating from one surface to the other surface in the thickness direction of the perforated sheet 50.
- the holes are formed substantially parallel to the thickness direction of the perforated sheet 50.
- the “through hole” is a hole whose outer periphery is surrounded by the base material of the perforated sheet 50 when the perforated sheet 50 is viewed in plan from the thickness direction. Good.
- the “through hole” is a hole in which a part of the outer periphery of the hole is not surrounded by the base material of the perforated sheet 50 when the perforated sheet 50 is viewed in plan from the thickness direction. There may be. “A hole in which a part of the outer periphery of the hole is not surrounded by the base material of the perforated sheet 50” means that when the perforated sheet 50 is viewed in plan from the thickness direction, the end of the perforated sheet 50 is inward. It includes a hole extending in a slit shape. In the present embodiment, the shape of the “through hole” is not particularly limited.
- the perforated sheet 50 is provided with a plurality of through holes A having a hole area of 0.5 mm 2 or more.
- Each hole area of the through hole A is preferably 1 mm 2 or more, may be 10 mm 2 or more.
- each hole area of the through hole A may be 600 mm 2 or less, or 200 mm 2 or less.
- the sizes of the plurality of through holes A may be the same as or different from each other.
- the shape of the through hole A (the shape when viewed from one side in the thickness direction) is not particularly limited, and is, for example, a circle, a rectangle, a triangle, or the like.
- a circular through hole A having a hole diameter (diameter) of 1 mm or more and 20 mm or less may be formed. Thereby, the tensile strength of the perforated sheet 50 is ensured more reliably.
- the perforated sheet 50 is formed with 15 to 15000 through holes A per 100 cm 2 .
- the aperture ratio in the perforated sheet 50 is different between the upper part and the lower part.
- the aperture ratio of the perforated sheet 50 may be higher than the aperture ratio of the lower part.
- the perforated sheet 50 may have a lower opening ratio than a top opening ratio.
- the “upper portion” is a portion from the upper end to the lower side by 30% with respect to the vertical length of the perforated sheet 50 (the vertical length in the region sandwiched between the positive electrode plate 20 and the negative electrode plate 30).
- the “lower part” is a part up to 30% in length upward from the lower end.
- the part sandwiched between the upper part and the lower part is also simply referred to as “middle part” below.
- “upper” and “lower” because “upper” and “lower” means that the direction from the bottom surface of the battery case 60 of the lead storage battery 1 to the opening (the lid 62) is upward, Based on “upper” and “lower” when the opposite direction is the lower direction.
- the vertical direction corresponds to the direction of gravity when the lead storage battery 1 is placed on an automobile or the like.
- the aperture ratio of the perforated sheet 50 is obtained as follows. Specifically, in a state where the perforated sheet 50 is viewed in plan from the thickness direction, the perforated sheet is divided into a square region by dividing the perforated sheet in the vertical direction (vertical direction) and the direction perpendicular to the vertical direction (lateral direction) at intervals of 5 mm. Divide (divide into square grids with sides of 5 mm). In each divided area, the area ratio (%) occupied by the holes in each area is measured. The aperture ratio is obtained by calculating the average value of the area ratio occupied by the holes in each region measured in a plurality of regions. The aperture ratio is obtained for each of the upper part and the lower part.
- the aperture ratio is the aperture ratio in each divided area obtained by dividing the perforated sheet 50 into a square grid area having a side of 5 mm in a state where the perforated sheet 50 is viewed from the thickness direction.
- a certain area opening ratio is measured, and is an arithmetic average of all the measured area opening ratios.
- the measurement of the aperture ratio can also be performed using image processing.
- the area ratio occupied by the holes may be measured for all of the plurality of regions included in the part, and the aperture ratio may be obtained from the average value. It is not limited.
- the area ratio occupied by the holes may be measured for a plurality of regions at the same height position (vertical direction position), and the average value may be used as the aperture ratio of the region.
- a perforated sheet 50 in which a plurality of through holes A are formed is disposed between the positive electrode plate 20 and the negative electrode plate 30. Therefore, while the positive electrode plate 20 and the negative electrode plate 30 are insulated by the perforated sheet 50, the electrolytic solution moves from one surface of the perforated sheet 50 to the other surface via the through hole A, and The electrolyte can move up and down along the other surface.
- the aperture ratio of the perforated sheet 50 is further different between the upper part and the lower part. Therefore, as will be described in detail below, durability after repeated charge and discharge can be improved.
- the current distribution of the electrode plate can be made closer to uniform during discharge. This is because, during discharge, discharge tends to proceed preferentially in the lower portions of the positive electrode plate 20 and the negative electrode plate 30.
- the perforated sheet 50 having a lower aperture ratio in the lower part the current flowing in the vertical direction can be suppressed in the lower part. As a result, it is estimated that the current distribution in the vertical direction can be made more uniform in each of the positive electrode plate 20 and the negative electrode plate 30.
- the perforated sheet 50 having an opening ratio larger at the lower portion than at the upper portion is used, the current distribution of the electrode plate can be made to be uniform in charging.
- the difference between the upper opening ratio (%) and the lower opening ratio (%) is preferably 15 points or more, and more preferably 20 points or more. Further, the difference between the upper opening ratio (%) and the lower opening ratio (%) may be 50 points or less, or 40 points or less.
- the opening ratio (%) in the middle part may be the same as either the opening ratio (%) in the upper part or the opening ratio (%) in the lower part, or the opening ratio (%) in the upper part and the lower part. It may be a value between the aperture ratio (%).
- the difference between the upper aperture ratio (%) and the lower aperture ratio (%) is 15 points or more, so that the current distribution of the electrode plate in charge and discharge can be made more uniform, and durability against repeated charge and discharge. Can be further improved.
- the aperture ratio (%) may be 30% or more in either the upper part or the lower part where the aperture ratio (%) is higher.
- the aperture ratio of either the upper part or the lower part having a higher aperture ratio is 30% or more, the current distribution of the electrode plate in charge / discharge can be made more uniform, and durability against repeated charge / discharge can be further improved. Can be improved.
- the aperture ratio (%) may be 40% or less in either the upper part or the lower part where the aperture ratio (%) is lower.
- the upper opening ratio (%) when the upper opening ratio (%) is larger than the lower opening ratio (%), the upper opening ratio (%) is, for example, 30% or more and 80% or less.
- the opening ratio (%) of the lower part is, for example, 0% or more and 40% or less.
- the upper opening ratio (%) when the lower opening ratio (%) is larger than the upper opening ratio (%), the upper opening ratio (%) is, for example, 0% as shown in FIG.
- the opening ratio (%) of the lower part is, for example, 30% or more and 80% or less.
- the perforated sheet a plurality of through holes having a hole area of 1 mm 2 or more are formed, and the difference between the upper opening ratio (%) and the lower opening ratio (%) is different as described above.
- the aperture ratio (%) is preferably in the above numerical range.
- the portion other than the through hole A in the perforated sheet 50 is porous and can hold the electrolytic solution.
- the perforated sheet 50 is, for example, a nonwoven fabric in which through holes are formed.
- the material of the perforated sheet 50 may be polyolefin such as polyethylene or polypropylene, or polyester.
- the perforated sheet 50 may be a polyolefin nonwoven fabric in which the through-holes A are formed.
- the perforated sheet 50 may be a sheet formed of glass fiber or cellulose fiber.
- the perforated sheet 50 is disposed between the negative electrode plate 30 and the separator 40.
- the durability against repeated charge / discharge can be further improved as compared with the case where the perforated sheet 50 is disposed between the positive electrode plate 20 and the separator 40. it can. This is because the current bias is more easily caused by the negative electrode plate 30 than by the positive electrode plate 20, and the effect of equalizing the current is obtained by bringing the perforated sheet 50 closer to the negative electrode plate 30. Infer.
- the positive electrode plate 20 includes a metal positive electrode current collector 21 and a positive electrode material 22 attached to the positive electrode current collector 21.
- the positive electrode current collector 21 includes a lattice-shaped lattice portion, an upper frame bone disposed along the upper end portion of the lattice portion, and an ear portion protruding upward from a part of the upper portion of the upper frame bone.
- the positive electrode plate 20 is formed by filling the lattice portion with the positive electrode material 22. In the positive electrode plate 20, the positive electrode material 22 adheres to almost all of the lattice portions, and the positive electrode material 22 does not adhere to the ear portions. By connecting the ears of the positive electrode plates 20 via the positive electrode strap 71, the plurality of positive electrode plates 20 are electrically connected in parallel.
- the positive electrode current collector 21 is formed by, for example, an expanding process.
- the ear part of the positive electrode current collector 21 has a flat plate shape and protrudes upward from a part of the upper frame bone.
- the upper part of the ear part is disposed below the liquid surface of the electrolytic solution.
- the positive electrode current collector 21 is made of lead (Pb) or a lead alloy (made of Pb alloy) containing lead (Pb) and a metal other than lead, for example.
- the positive electrode current collector 21 may be made of a Pb—Ca—Sn alloy.
- the positive electrode current collector 21 may be formed by processing one metal plate.
- the material of the lattice portion and the material of the ear portion may be the same.
- the positive electrode material 22 includes an active material made of particulate lead dioxide.
- the positive electrode material 22 may contain elements other than reinforcing fibers and Pb.
- the positive electrode material 22 includes particles containing lead dioxide (PbO 2 ) as an active material. Since a part of lead dioxide changes to lead sulfate along with discharge, the above particles may contain lead sulfate during charging and discharging.
- PbO 2 lead dioxide
- Examples of reinforcing fibers that can be included in the positive electrode material 22 include synthetic resin fibers.
- the negative electrode plate 30 has a metal negative electrode current collector 31 and a negative electrode material 32 attached to the negative electrode current collector 31.
- the structure of the negative electrode current collector 31 is the same as that of the positive electrode current collector 21.
- the negative electrode material 32 may contain an additive in addition to the active material, and may contain an organic shrinkage agent, a carbon material such as carbon black, and / or barium sulfate as the additive. .
- the negative electrode material 32 includes particles containing metallic lead (Pb) as an active material. Since a part of lead changes to lead sulfate with discharge, the above particles may contain lead sulfate during charging and discharging.
- Pb metallic lead
- the organic shrinkage agent as the additive is, for example, lignin (sulfonic acid), bisphenol formaldehyde condensate or the like.
- the negative electrode material 32 may contain 0% by mass or more and 1% or less of an organic shrinkage agent.
- Examples of the carbon material include graphite such as natural graphite and artificial graphite, carbon black such as ketjen black (registered trademark) and acetylene black, and carbon nanotube.
- the separator 40 is porous and holds the electrolytic solution therein.
- the separator 40 is an insulating member.
- the separator 40 prevents a short circuit between the positive electrode plate 20 and the negative electrode plate 30 while holding the electrolytic solution.
- the separator 40 may be formed in a bag shape and may be disposed in the electrode plate group 10 in a state of wrapping either the positive electrode plate 20 or the negative electrode plate 30.
- the separator 40 is, for example, a microporous film, a woven fabric, or a non-woven fabric.
- the material of the separator 40 include a polymer compound, glass, and ceramic.
- the polymer compound include polyolefin (PO) such as polypropylene (PP) and polyethylene (PE).
- PO polyolefin
- PP polypropylene
- PE polyethylene
- the separator 40 may include an inorganic filler, carbon particles, and the like.
- the electrolytic solution is an aqueous solution of sulfuric acid.
- the density of the electrolyte in a fully charged state (20 ° C.) may be 1.20g / cm 3 ⁇ 1.35g / cm 3.
- the electrolytic solution contains at least sulfuric acid.
- the electrolytic solution may further contain aluminum ions, sodium ions, and the like.
- the positive electrode plate 20 is produced by filling the positive electrode current collector 21 with a positive electrode paste containing lead powder.
- the negative electrode plate 30 is produced by filling the negative electrode current collector 31 with a negative electrode paste containing lead powder.
- seat 50 is produced, for example by forming the some through-hole A in a nonwoven fabric.
- the positive electrode plate 20, the separator 40, the perforated sheet 50, and the negative electrode plate 30 are laminated to form the electrode plate group 10.
- the lead storage battery 1 is assembled by placing the plurality of electrode plate groups 10 in the case body 61 of the battery case 60, closing the opening of the case body 61 with the lid portion 62, and putting the electrolytic solution in the battery case 60. Finally, chemical conversion is performed on the assembled lead-acid battery 1.
- the grid portion of the positive electrode current collector 21 is filled with a positive electrode paste containing lead powder.
- the positive electrode paste at the time of filling is prepared by kneading lead powder and additives with dilute sulfuric acid.
- the mass of the positive electrode material 22 can be adjusted by changing the filling amount of the positive electrode paste into the lattice portion of the positive electrode current collector 21.
- a method for filling the positive electrode paste a general method is adopted. After filling, an aging process is performed, and a drying process is further performed.
- the negative electrode plate 30 is produced in the same manner as the production of the positive electrode plate 20 described above.
- the separator 40 what is marketed can be used as the separator 40.
- the perforated sheet 50 for example, through holes A are formed in the thickness direction in a non-woven fabric made of polyolefin by punching. By appropriately adjusting the size and number of the through holes A, the perforated sheet 50 is produced so that the upper and lower portions have predetermined opening ratios.
- the plurality of positive electrode plates 20 are arranged so that the positive electrode plates 20 and the negative electrode plates 30 are alternately arranged in one direction and the separators 40 are sandwiched between the positive electrode plates 20 and the negative electrode plates 30. And a plurality of separators 40 and a plurality of negative electrode plates 30 are laminated to form a laminate.
- the perforated sheet 50 is disposed between the separator 40 and the negative electrode plate 30.
- the positive electrode straps 71 electrically connect the positive electrode plates 20 in parallel.
- the negative electrode straps 81 electrically connect the plurality of negative electrode plates 30 in parallel.
- the electrolytic solution is prepared, for example, by adding sulfuric acid to water and mixing. By changing the amount of sulfuric acid to be added, the density of the electrolyte can be adjusted.
- a plurality of electrode plate groups 10 are placed in the case body 61 of the battery case 60.
- the electrode plate group 10 is accommodated in each cell chamber of the case body 61 partitioned by the partition walls.
- the plurality of electrode plate groups 10 are electrically connected in series by the connecting member 90.
- the electrolytic solution is put into the case main body 61.
- the lead storage battery 1 manufactured as described above is used, for example, as a battery for automobiles, forklifts, and the like.
- the use and size of the lead storage battery 1 are not particularly limited.
- the lead acid battery of this invention is not limited to the said embodiment, Of course, various changes can be added within the range which does not deviate from the summary of this invention.
- the configuration of another embodiment can be added to the configuration of a certain embodiment, and a part of the configuration of a certain embodiment can be replaced with the configuration of another embodiment.
- a part of the configuration of an embodiment can be deleted.
- the so-called paste-type positive electrode plate 20 has been described in detail, but in the present invention, the positive electrode may be of a clad type.
- a lead-acid battery was manufactured as shown below.
- Test Example 1 Preparation of positive electrode (positive electrode plate) Lead powder and dilute sulfuric acid were mixed to prepare a positive electrode paste. The prepared positive electrode paste was filled in the grid portion of the current collector and aged. Further, a plurality of positive electrode plates were produced by drying.
- Electrolytic Solution As an electrolytic solution, an aqueous sulfuric acid solution having a density (20 ° C.) of 1.280 g / cm 3 was prepared.
- Test Examples 2 to 7 As shown in Table 1, a battery was manufactured in the same manner as in Test Example 1 except that the aperture ratio of the perforated sheet was changed or the perforated sheet was not used.
- Test Examples 8 to 14 As shown in Table 2, a battery was manufactured in the same manner as in Test Example 1 except that the aperture ratio of the perforated sheet was changed or the perforated sheet was not used.
- the battery of the test example in which the change width of the electrode plate potential difference is reduced by 20% or more with respect to the change width of the electrode plate potential difference of such a battery is A, less than 20% and The battery of the test example that decreased by 10% or more was determined as B, and the battery of the test example that decreased by less than 10% was determined as C.
- Such a determination was based on the average value of the change width of the electrode plate potential difference through the entire charge / discharge cycle.
- Tables 1 and 2 show the results of the evaluation test of the uniformity of the current distribution.
- FIG. 4 shows a graph showing an example of the measurement result of the potential difference over time in such an evaluation test.
- a perforated sheet for example, a non-woven fabric
- a perforated sheet for example, a non-woven fabric
- the nonwoven fabric is porous and can be impregnated with an electrolytic solution, even if the nonwoven fabric is disposed between the positive electrode plate and the negative electrode plate, the charge / discharge reaction between the positive electrode plate and the negative electrode plate proceeds without being suppressed so much. In other words, the charge / discharge reaction between the positive electrode plate and the negative electrode plate proceeds even through a portion where a hole is not formed (non-penetrating portion).
- the charge / discharge reaction proceeds more sufficiently through the through-hole by forming the through-hole.
- the current flowing between the positive electrode plate and the negative electrode plate does not necessarily flow between the same height portions of the electrode plates, but also flows between different height portions.
- the current tends to concentrate toward the upper part of the negative electrode, and in the initial stage of charging, the current tends to flow toward the lower part of the negative electrode. Therefore, the charge / discharge current flows in a biased direction either upward or downward.
- the flow of current between the plates in the vertical direction that is, the movement of ions in the electrolyte in the vertical direction
- It can be limited on the lower side than the higher side.
- Charging / discharging by placing the one with a lower aperture ratio of the perforated sheet (either the upper part or the lower part of the perforated sheet) on the one where charge / discharge reaction is likely to occur (for example, either the upper part or the lower part of the electrolyte)
- the current bias can be made uniform. Thereby, it is thought that the charging / discharging reaction in the path
- the aperture ratio of the perforated sheet when the aperture ratio of the perforated sheet is high at the top and low at the bottom, the movement of ions in the electrolyte in the vertical direction is restricted at the bottom rather than the top.
- the current concentrates toward the upper part of the negative electrode plate for example, during discharge
- the current flowing from the lower part of the positive electrode plate to the upper part of the negative electrode plate can be suppressed. Therefore, it is considered that the current distribution can be made close to uniform.
- the aperture ratio of the perforated sheet when the aperture ratio of the perforated sheet is high at the lower part and low at the upper part, the movement of ions in the electrolytic solution in the upper and lower direction is restricted above the lower part.
- the current distribution can be made close to uniform.
- the charge / discharge reaction between the positive electrode active material and the negative electrode active material facing each other through the non-penetrating portion of the nonwoven fabric easily proceeds by way of the through hole. Specifically, even if the active material of one electrode plate and the active material of the other electrode plate are at the same height position and there is a non-penetrating part between these active materials, The reaction proceeds with the active material through a through hole, for example, in a detour path.
- the reaction proceeds through a through hole, for example, along a path inclined upward and downward.
- the presence / absence of the through-hole facilitates the charge / discharge reaction between the positive electrode plate and the negative electrode plate not only in the path between the same height but also in the path between the different heights. Therefore, it is considered that the current distribution in the vertical direction, which tends to be non-uniform, can be made closer to uniform and cycle durability is improved.
- the difference between the opening ratio (%) of the upper part of the perforated sheet and the opening ratio (%) of the lower part is 15 points or more, so that the opening ratio of the upper part is When it is high, the charge / discharge distribution can be made uniform even in the discharge (Table 1). On the other hand, when the opening ratio at the lower part is high, the charge / discharge distribution can be made uniform even in charging (Table 2).
- Test Examples 15 to 17 As shown in Table 3, the battery was fabricated in the same manner as in Test Example 1 except that the hole area (per one) of the through holes of the perforated sheet was changed or the perforated sheet was not used. Manufactured.
- the electrolyte solution is stratified by arranging a perforated sheet in which through holes are formed and the opening ratios are different between the upper part and the lower part between the positive electrode plate and the negative electrode plate.
- Test Example 16 it is considered that the current distribution can be made closer to uniform as described above by using perforated sheets having different opening ratios at the upper part and the lower part.
- concentration difference in the vertical direction of the electrolytic solution can be suppressed, and it is considered that stratification can be suppressed. It is considered that durability against repeated charge / discharge can be improved by suppressing stratification.
- Table 4 below shows the results of evaluating the durability against repeated charge and discharge in the same manner as described above using the lead storage battery in which the arrangement of the perforated sheet of Test Example 1 was changed (Test Example 1 ′). Specifically, when the perforated sheets arranged on the positive electrode plate and the negative electrode plate are arranged on the negative electrode plate side with respect to the separator (negative electrode side), and on the positive electrode plate side with respect to the separator (positive electrode side) Table 4 shows the results. As can be seen from Table 4, by disposing the perforated sheet on the negative electrode side, durability against repeated charge / discharge can be further improved.
- Electrode plate group 20: positive electrode plate (positive electrode), 21: positive electrode current collector, 22: positive electrode material, 30: Negative electrode plate (negative electrode), 31: Negative electrode current collector, 32: Negative electrode material, 40: Separator, 50: Perforated sheet, A: Through hole, 60: Battery case (case), 61: Case body, 62: Cover part, 70: positive electrode terminal, 71: strap for positive electrode, 80: negative electrode terminal, 81: strap for negative electrode, 90: connecting member, 91: liquid spout.
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Abstract
Description
本発明は、鉛蓄電池に関する。 The present invention relates to a lead storage battery.
従来、正極板と、負極板と、正極板と負極板との間に配置されたセパレータと、電解液と、正極板と負極板とセパレータと電解液とを収容する電槽と、を備えた鉛蓄電池が知られている(例えば、特許文献1)。 Conventionally, a positive electrode plate, a negative electrode plate, a separator disposed between the positive electrode plate and the negative electrode plate, an electrolytic solution, and a battery case that accommodates the positive electrode plate, the negative electrode plate, the separator, and the electrolytic solution are provided. A lead storage battery is known (for example, Patent Document 1).
特許文献1に記載の鉛蓄電池では、負極板の表面には、膜体が付設され、膜体は、基材と、基材の表面を覆う親水被膜と、を有し、親水被膜は、親水材料と、保持体材料と、を含み、親水材料は、アルミナ又はシリカを含み、保持体材料は、アクリルアミド、シリカゾル又はシランカップリング剤であり、基材の空孔率(隙間の割合)は、負極板の上部の方が負極板の下部よりも高い。
In the lead storage battery described in
特許文献1に記載の鉛蓄電池では、繰り返し充放電に対する耐久性が良好でない場合がある。
In the lead storage battery described in
本実施形態は、繰り返し充放電に対する耐久性が向上された鉛蓄電池を提供することを課題とする。 This embodiment makes it a subject to provide the lead storage battery with which durability with respect to repeated charging / discharging was improved.
本実施形態の鉛蓄電池は、正極板と、負極板と、正極板及び負極板の間に配置され且つ厚さ方向に貫通孔が形成された孔あきシートと、電解液とを含み、孔あきシートにおける開口率は、上部と下部とで異なる。
上記の構成により、繰り返し充放電に対する耐久性を向上させることができる。
The lead storage battery of the present embodiment includes a positive electrode plate, a negative electrode plate, a perforated sheet disposed between the positive electrode plate and the negative electrode plate and having a through-hole formed in the thickness direction, and an electrolyte solution. The aperture ratio is different between the upper part and the lower part.
With the above configuration, durability against repeated charge and discharge can be improved.
以下、本発明に係る鉛蓄電池の一実施形態について、図1~図3を参照しつつ説明する。尚、本実施形態の各構成部材(各構成要素)の名称は、本実施形態におけるものであり、背景技術における各構成部材(各構成要素)の名称と異なる場合がある。 Hereinafter, an embodiment of a lead storage battery according to the present invention will be described with reference to FIGS. 1 to 3. In addition, the name of each component (each component) of this embodiment is a thing in this embodiment, and may differ from the name of each component (each component) in background art.
本実施形態の鉛蓄電池1は、硫酸水溶液を電解液として含み、二酸化鉛もしくは硫酸鉛を正極の活物質として有し、金属鉛もしくは硫酸鉛を負極の活物質として有する鉛蓄電池である。鉛蓄電池1は、放電時に電気エネルギーを外部へ供給し、充電時に電気エネルギーを内部に蓄積する。
The
鉛蓄電池1は、図1に示すように、電槽60(ケース)と、電槽60(ケース)の内部に収容された電解液と、電解液に浸かった状態の複数の極板群10と、を含む。鉛蓄電池1は、さらに、正極端子70と、負極端子80と、複数の極板群10同士を電気的に直列に接続する接続部材90と、を含む。鉛蓄電池1は、正極端子70及び負極端子80を介して、複数の極板群10に貯められた電気エネルギーを外部へ供給したり、複数の極板群10に外部からの電気エネルギーを貯めたりするように構成されている。本実施形態の鉛蓄電池1は、液式鉛蓄電池である。
As shown in FIG. 1, the lead-
電槽60(ケース)は、長方形状の底面を有する直方体状である。電槽60(ケース)は、上方に向けて開口したケース本体61と、ケース本体61の開口を塞ぐ蓋部62とを備える。ケース本体61は、内部空間が隔壁によって仕切られて形成された複数のセル室を有する。複数のセル室は、底面の長辺方向と同じ方向(水平方向)に並んでいる。各セル室には、電解液と、1つの極板群10とが収容されている。蓋部62は、電池内部で発生したガスを電池外へ排出できる液口栓91を有する。
The battery case 60 (case) has a rectangular parallelepiped shape having a rectangular bottom surface. The battery case 60 (case) includes a case
各極板群10は、複数の正極板20(正極)と、複数の負極板30(負極)と、正極板20及び負極板30を物理的に隔離させるための複数のセパレータ40と、正極板20同士を電気的に並列に接続する正極用ストラップ71と、負極板30同士を電気的に並列に接続する負極用ストラップ81と、を有する。図2に示すように、各極板群10は、正極板20及び負極板30の間に配置され且つ厚さ方向に貫通孔Aが形成された孔あきシート50をさらに有する。各極板群10では、複数の正極板20と、複数のセパレータ40と、複数の負極板30とが厚さ方向に積層されている。各極板群10の正極板20及び負極板30の厚さ方向(積層方向)は、電槽60(ケース)において複数の極板群10が並ぶ方向と、同じ方向である。なお、セパレータ40は、正極板20及び負極板30の間に配置されている。
Each
鉛蓄電池1では、互いに隣り合う極板群10のうち、一方の極板群10の正極用ストラップ71と、他方の極板群10の負極用ストラップ81とが、上記の接続部材90によって接続されることによって、複数の極板群10が、電気的に直列に接続されている。
In the
孔あきシート50は、正極板20とセパレータ40との間、又は、負極板30とセパレータ40との間に配置される。孔あきシート50は、電解液を含浸する多孔質な基材で形成されている。図3に示すように、孔あきシート50には、厚さ方向に貫通する複数の貫通孔Aが形成されている。貫通孔Aが形成されていな部分のセパレータ40の厚さは、厚さ方向に圧縮されていない状態で、0.01mm以上2.0mm以下であってもよい。
本実施形態において、「貫通孔」とは、孔あきシート50の厚さ方向において、一方の面から他方の面まで貫通する孔を意味する。当該孔は、孔あきシート50の厚さ方向に略平行に形成されているものとする。
The
In the present embodiment, the “through hole” means a hole penetrating from one surface to the other surface in the thickness direction of the perforated
なお、本実施形態において、「貫通孔」とは、孔あきシート50を厚さ方向から平面視した場合に、孔の外周が孔あきシート50の基材により囲われている孔であってもよい。また、本実施形態において、「貫通孔」とは、孔あきシート50を厚さ方向から平面視した場合に、孔の外周の一部が孔あきシート50の基材により囲われていない孔であってもよい。「孔の外周の一部が孔あきシート50の基材により囲われていない孔」とは、孔あきシート50を厚さ方向から平面視した場合に、孔あきシート50の端部から内側に向かってスリット状に延びる孔を含む。なお、本実施形態において、「貫通孔」の形状は、特に限定されるものではない。
In the present embodiment, the “through hole” is a hole whose outer periphery is surrounded by the base material of the
例えば、孔あきシート50には、孔面積が0.5mm2以上の複数の貫通孔Aが穿設されている。貫通孔Aの各孔面積は、1mm2以上であることが好ましく、10mm2以上であってもよい。また、貫通孔Aの各孔面積は、600mm2以下であってもよく、200mm2以下であってもよい。なお、複数の貫通孔Aの大きさは、互いに同じであっても、異なっていてもよい。
貫通孔Aの孔面積が1mm2以上であることによって、繰り返し充放電後の電解液の比重差をより小さくすることができる。また、貫通孔Aの孔面積が200mm2以下であることによって、繰り返し充放電後の電解液の比重差をより小さくすることができる。
For example, the perforated
When the hole area of the through-hole A is 1 mm 2 or more, the specific gravity difference of the electrolytic solution after repeated charge and discharge can be further reduced. Moreover, when the hole area of the through-hole A is 200 mm < 2 > or less, the specific gravity difference of the electrolyte solution after repeated charging / discharging can be made smaller.
貫通孔Aの形状(厚さ方向の一方側から見たときの形状)は、特に限定されないが、例えば、円形、矩形、三角形などである。孔あきシート50には、孔径(直径)が1mm以上20mm以下の円形の貫通孔Aが形成されてもよい。これにより、孔あきシート50の引張強度が、より確実に確保される。例えば、孔あきシート50には、100cm2あたり、貫通孔Aが、15個以上15000個以下形成されている。
The shape of the through hole A (the shape when viewed from one side in the thickness direction) is not particularly limited, and is, for example, a circle, a rectangle, a triangle, or the like. In the perforated
孔あきシート50における開口率は、上部と下部とで異なる。換言すれば、 孔あきシート50は、上部の開口率が、下部の開口率よりも高くなっていてもよい。また、孔あきシート50は、下部の開口率が、上部の開口率よりも高くなっていてもよい。
「上部」は、孔あきシート50の上下方向長さ(正極板20及び負極板30に挟まれた領域における上下方向長さ)に対して、上端から下方へ30%長さまでの部分である。一方、「下部」は、下端から上方へ30%長さまでの部分である。なお、上部と下部との間に挟まれた部分を、以下で単に「中部」ともいう。また、本実施形態において、「上部」および「下部」ので「上」および「下」とは、鉛蓄電池1の電槽60の底面から開口部(蓋部62)への方向を上方向とし、その逆方向を下方向とし場合における、「上」および「下」に基づく。なお、上下方向は、鉛蓄電池1が、自動車等に載置された場合における、重力方向に相当する。
The aperture ratio in the
The “upper portion” is a portion from the upper end to the lower side by 30% with respect to the vertical length of the perforated sheet 50 (the vertical length in the region sandwiched between the
孔あきシート50の開口率は、下記のようにして求められる。詳しくは、孔あきシート50を厚さ方向から平面視した状態において、5mm間隔で上下方向(縦方向)及び上下方向に垂直な方向(横方向)に孔あきシートを分割して正方形の領域に区分けする(一辺5mmの正方形の格子に分割する)。区分けした各領域において、各領域内の孔の占める面積割合(%)を測定する。複数の領域で測定した各領域における孔の占める面積割合の平均値を算出することによって、開口率を求める。上部及び下部のそれぞれについて、開口率を求める。
換言すれば、開口率とは、孔あきシート50を、厚さ方向から平面視した状態において、孔あきシートを一辺5mmの正方形の格子状の領域に分割し、分割した各領域における開口率である領域開口率を測定し、測定したすべての領域開口率の算術平均である。
The aperture ratio of the
In other words, the aperture ratio is the aperture ratio in each divided area obtained by dividing the
開口率の測定は、画像処理を用いても実施できる。なお、ある部分における開口率の測定方法は、当該部分に含まれる複数の領域のすべてに対して、孔の占める面積割合を測定し、その平均値から開口率を求めてもよいが、これに限られるものではない。例えば、ある部分において、同じ高さ位置(上下方向位置)の複数の各領域に対して、孔の占める面積割合を測定し、その平均値を当該領域の開口率としてもよい。 The measurement of the aperture ratio can also be performed using image processing. As for the method for measuring the aperture ratio in a certain part, the area ratio occupied by the holes may be measured for all of the plurality of regions included in the part, and the aperture ratio may be obtained from the average value. It is not limited. For example, in a certain part, the area ratio occupied by the holes may be measured for a plurality of regions at the same height position (vertical direction position), and the average value may be used as the aperture ratio of the region.
本実施形態においては、複数の上記貫通孔Aが形成された孔あきシート50が、正極板20及び負極板30の間に配置されている。このため、正極板20及び負極板30が孔あきシート50によって絶縁されつつ、電解液は、貫通孔Aを介して、孔あきシート50の一方の面から他方の面へ向けて移動し、さらに、電解液が他方の面に沿って上下方向に移動できる。
本実施形態においては、さらに、孔あきシート50における開口率が、上部と下部とで異なる。従って、下記に詳しく説明するように、繰り返し充放電後の耐久性を向上させることができる。
開口率が下部よりも上部で大きい孔あきシート50を用いた場合には、放電時において極板の電流分布を均一に近づけることができる。これは、放電時においては、正極板20及び負極板30のそれぞれの下部において、優先的に放電が進みやすいためである。下部において開口率がより低い孔あきシート50を設けることで、上下方向に流れる電流を下部において抑制することができる。その結果、正極板20及び負極板30のそれぞれにおいて、上下方向の電流分布をより均一にすることが可能になると推測される。
一方、開口率が上部よりも下部で大きい孔あきシート50を用いた場合には、充電時において極板の電流分布を均一に近づけることができる。これは、充電時においては、正極板20及び負極板30のそれぞれの上部において、優先的に充電が進みやすいためである。上部において開口率がより低い孔あきシート50を設けることで、上下方向に流れる電流を上部において抑制することができる。その結果、正極板20及び負極板30のそれぞれにおいて、上下方向の電流分布をより均一にすることが可能となると推測される。
このように、充電時及び放電時の両方における極板の電流分布を均一に近づけることによって、繰り返し充放電後の耐久性を向上させることができる。
In the present embodiment, a
In the present embodiment, the aperture ratio of the
In the case where the
On the other hand, when the
Thus, the durability after repeated charging and discharging can be improved by making the current distribution of the electrode plate both uniform during charging and discharging uniform.
孔あきシート50において、上部の開口率(%)と下部の開口率(%)との差は、15ポイント以上であることが好ましく、20ポイント以上であることがより好ましい。また、上部の開口率(%)と下部の開口率(%)との差は、50ポイント以下であってもよく、40ポイント以下であってもよい。なお、中部の開口率(%)は、上部の開口率(%)又は下部の開口率(%)のいずれか一方と同じであってもよく、あるいは、上部の開口率(%)と下部の開口率(%)との間における値であってもよい。
上部の開口率(%)と下部の開口率(%)との差が15ポイント以上であることによって、充放電における極板の電流分布をより均一に近づけることができ、繰り返し充放電に対する耐久性をより向上させることができる。
In the
The difference between the upper aperture ratio (%) and the lower aperture ratio (%) is 15 points or more, so that the current distribution of the electrode plate in charge and discharge can be made more uniform, and durability against repeated charge and discharge. Can be further improved.
孔あきシート50において、開口率(%)がより高い上部又は下部のいずれか一方では、開口率(%)は、30%以上であってもよい。開口率がより高い上部及び下部のいずれか一方の開口率が、30%以上であることによって、充放電における極板の電流分布をより均一に近づけることができ、繰り返し充放電に対する耐久性をより向上させることができる。一方、開口率(%)がより低い上部又は下部のいずれか一方では、開口率(%)は、40%以下であってもよい。
In the
具体的には、孔あきシート50において、下部の開口率(%)よりも上部の開口率(%)の方が大きい場合、上部の開口率(%)は、例えば、30%以上80%以下であり、下部の開口率(%)は、例えば、0%以上40%以下である。
一方、孔あきシート50において、図3に示すように、上部の開口率(%)よりも下部の開口率(%)の方が大きい場合、上部の開口率(%)は、例えば、0%以上40%以下であり、下部の開口率(%)は、例えば、30%以上80%以下である。
孔あきシートにおいて、孔面積が1mm2以上の複数の貫通孔が穿設され、上部の開口率(%)と下部の開口率(%)との差が上記のごとく異なり、上部及び下部の各開口率(%)が上記の数値範囲であることが好ましい。
Specifically, in the
On the other hand, in the
In the perforated sheet, a plurality of through holes having a hole area of 1 mm 2 or more are formed, and the difference between the upper opening ratio (%) and the lower opening ratio (%) is different as described above. The aperture ratio (%) is preferably in the above numerical range.
孔あきシート50における貫通孔A以外の部分は、多孔質であり、電解液を保持できる。孔あきシート50は、例えば、貫通孔が形成された不織布である。孔あきシート50の材質は、ポリエチレンやポリプロピレンなどのポリオレフィン、又は、ポリエステルであってもよい。具体的には、孔あきシート50は、貫通孔Aが形成されたポリオレフィン製の不織布であってもよい。孔あきシート50は、ガラス繊維やセルロース繊維で形成されたシートであってもよい。
The portion other than the through hole A in the
本実施形態では、孔あきシート50は、負極板30とセパレータ40との間に配置される。孔あきシート50が負極板30とセパレータ40との間に配置されることによって、正極板20とセパレータ40との間に配置された場合よりも、繰り返し充放電に対する耐久性をより向上させることができる。これは、電流の偏りが、正極板20よりも負極板30に起因しやすいためであり、孔あきシート50をより負極板30に近接させることで、電流の均一化の効果が得られたためと推測する。
In this embodiment, the
正極板20は、金属製の正極集電体21と、該正極集電体21に付着した正極電極材料22とを有する。正極集電体21は、格子状の格子部と、格子部の上端部に沿って配置された上部枠骨と、該上部枠骨の上部の一部から上方へ突出した耳部とを有する。正極板20は、格子部に正極電極材料22が充填されることによって形成されている。正極板20において、格子部のほぼ全てに正極電極材料22が付着し、耳部には正極電極材料22が付着していない。正極板20の耳部同士が上記の正極用ストラップ71を介して接続されることによって、複数の正極板20が電気的に並列に接続されている。
The
正極集電体21は、例えばエキスパンド加工によって形成されている。
The positive electrode
正極集電体21の耳部は、平板状であり、上部枠骨の一部から上方へ突出している。耳部の上部は、電解液の液面よりも下方に配置されている。
The ear part of the positive electrode
正極集電体21は、例えば、鉛(Pb)製、あるいは、鉛(Pb)と鉛以外の金属とを含む鉛合金製(Pb合金製)である。具体的には、正極集電体21は、Pb-Ca-Sn合金製であってもよい。正極集電体21は、1枚の金属板が加工されて形成されてもよい。正極集電体21において、格子部の材質と、耳部の材質とは、同じであってもよい。
The positive electrode
正極電極材料22は、粒子状の二酸化鉛からなる活物質を含む。正極電極材料22は、補強用繊維やPb以外の元素を含んでもよい。
The
正極電極材料22は、活物質として、二酸化鉛(PbO2)を含有する粒子を含む。放電に伴って、二酸化鉛の一部が硫酸鉛に変化することから、上記の粒子は、充放電中において硫酸鉛を含有してもよい。
The
正極電極材料22に含まれ得る補強用繊維としては、合成樹脂製の繊維などが挙げられる。
Examples of reinforcing fibers that can be included in the
負極板30は、金属製の負極集電体31と、該負極集電体31に付着した負極電極材料32とを有する。負極集電体31の構造については、正極集電体21と同様である。負極電極材料32は、例えば、活物質以外に、添加剤を含有していてもよく、添加剤として、有機防縮剤、カーボンブラックなどの炭素材料、及び/又は硫酸バリウムなどを含有してもよい。
The
負極電極材料32は、活物質として、金属鉛(Pb)を含有する粒子を含む。放電に伴って、鉛の一部が硫酸鉛に変化することから、上記の粒子は、充放電中において硫酸鉛を含有してもよい。
The
添加剤としての有機防縮剤は、例えば、リグニン(スルホン酸)、ビスフェノール類ホルムアルデヒド縮合物などである。負極電極材料32は、有機防縮剤を0質量%以上1%以下含有してもよい。
The organic shrinkage agent as the additive is, for example, lignin (sulfonic acid), bisphenol formaldehyde condensate or the like. The
炭素材料としては、例えば、天然黒鉛や人造黒鉛などの黒鉛、ケッチェンブラック(登録商標)やアセチレンブラックなどのカーボンブラック、カーボンナノチューブなどが挙げられる。 Examples of the carbon material include graphite such as natural graphite and artificial graphite, carbon black such as ketjen black (registered trademark) and acetylene black, and carbon nanotube.
セパレータ40は、多孔質であり、内部に電解液を保持する。セパレータ40は、絶縁性を有する部材である。セパレータ40は、電解液を保持しつつ、正極板20と負極板30と間の短絡を防いでいる。セパレータ40は、例えば、袋状に形成され、正極板20又は負極板30のいずれか一方を包み込んだ状態で、極板群10内に配置されてもよい。
The
セパレータ40は、例えば、微多孔膜、織布又は不織布である。セパレータ40の材質としては、高分子化合物、ガラス、セラミックなどが挙げられる。高分子化合物としては、例えば、ポリプロピレン(PP)、ポリエチレン(PE)などのポリオレフィン(PO)が挙げられる。セパレータ40は、無機フィラーやカーボン粒子などを含んでもよい。
The
電解液は、硫酸の水溶液である。満充電状態における電解液の密度(20℃)は、1.20g/cm3~1.35g/cm3であってもよい。電解液は、少なくとも硫酸を含む。電解液は、アルミニウムイオンやナトリウムイオンなどをさらに含んでもよい。
The electrolytic solution is an aqueous solution of sulfuric acid. The density of the electrolyte in a fully charged state (20 ° C.) may be 1.20g /
次に、上記実施形態の鉛蓄電池1の製造方法の一例について説明する。
Next, an example of a method for manufacturing the
鉛蓄電池1の製造方法では、まず、鉛粉を含む正極ペーストを正極集電体21に充填することによって正極板20を作製する。また、鉛粉を含む負極ペーストを負極集電体31に充填することによって負極板30を作製する。また、例えば不織布に複数の貫通孔Aを形成することによって、孔あきシート50を作製する。次に、正極板20、セパレータ40、孔あきシート50、及び負極板30を積層して極板群10を形成する。続いて、複数の極板群10を電槽60のケース本体61に入れ、ケース本体61の開口を蓋部62で塞ぎ、電解液を電槽60に入れることによって鉛蓄電池1を組み立てる。最後に、組み立てた鉛蓄電池1に対して、化成を行う。
In the manufacturing method of the
正極板20の作製では、正極集電体21の格子部に、鉛粉を含む正極ペーストを充填する。充填時の正極ペーストは、鉛粉及び添加剤を希硫酸で混練することで作製する。正極集電体21の格子部への正極ペーストの充填量を変化させることによって、正極電極材料22の質量を調整することができる。正極ペーストの充填方法としては、一般的な方法が採用される。充填後、熟成処理を行い、さらに乾燥処理を行う。
In the production of the
負極板30の作製では、上記の正極板20の作製と同様にして、負極板30を作製する。なお、セパレータ40としては、市販されているものを用いることができる。
In the production of the
孔あきシート50の作製では、例えば、打ち抜き加工によって、ポリオレフィン製の不織布に、厚さ方向に貫通孔Aを形成する。貫通孔Aの大きさや数などを適宜調整することによって、上部及び下部においてそれぞれ所定の開口率となるように、孔あきシート50を作製する。
In the production of the
極板群10の形成では、正極板20及び負極板30が交互に一方向に並ぶように、且つ、正極板20及び負極板30の間にセパレータ40が挟み込まれるように、複数の正極板20と複数のセパレータ40と複数の負極板30とを積層して、積層体を作る。このとき、例えば、セパレータ40と負極板30との間に孔あきシート50を配置する。正極用ストラップ71によって、複数の正極板20を電気的に並列に接続する。負極用ストラップ81によって、複数の負極板30を電気的に並列に接続する。
In the formation of the
電解液は、例えば、水に硫酸を加えて混合することによって調製する。加える硫酸の量を変えることによって、電解液の密度を調整できる。 The electrolytic solution is prepared, for example, by adding sulfuric acid to water and mixing. By changing the amount of sulfuric acid to be added, the density of the electrolyte can be adjusted.
鉛蓄電池1の組み立てでは、電槽60のケース本体61に複数の極板群10を入れる。隔壁によって仕切られたケース本体61の各セル室に、極板群10をそれぞれ収容する。接続部材90によって、複数の極板群10を電気的に直列に接続する。電解液をケース本体61内に入れる。
In assembling the
化成処理では、組み立てた鉛蓄電池1に対して、所定の電気量を通電する。
In the chemical conversion treatment, a predetermined amount of electricity is applied to the assembled
上記のようにして製造された鉛蓄電池1は、例えば、自動車やフォークリフトなどのバッテリーとして使用される。上記鉛蓄電池1の用途や大きさ、特に限定されない。
The
尚、本発明の鉛蓄電池は、上記実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。例えば、ある実施形態の構成に他の実施形態の構成を追加することができ、また、ある実施形態の構成の一部を他の実施形態の構成に置き換えることができる。さらに、ある実施形態の構成の一部を削除することができる。 In addition, the lead acid battery of this invention is not limited to the said embodiment, Of course, various changes can be added within the range which does not deviate from the summary of this invention. For example, the configuration of another embodiment can be added to the configuration of a certain embodiment, and a part of the configuration of a certain embodiment can be replaced with the configuration of another embodiment. Furthermore, a part of the configuration of an embodiment can be deleted.
例えば、上記実施形態では、いわゆるペースト式の正極板20について詳しく説明したが、本発明において、正極は、クラッド式のものであってもよい。
For example, in the above-described embodiment, the so-called paste-type
以下に示すようにして、鉛蓄電池を製造した。 A lead-acid battery was manufactured as shown below.
(試験例1)
(1)正極(正極板)の作製
鉛粉と希硫酸とを混合して、正極ペーストを調製した。調製した正極ペーストを、集電体の格子部に充填し、熟成させた。さらに乾燥させることによって、正極板を複数作製した。
(Test Example 1)
(1) Preparation of positive electrode (positive electrode plate) Lead powder and dilute sulfuric acid were mixed to prepare a positive electrode paste. The prepared positive electrode paste was filled in the grid portion of the current collector and aged. Further, a plurality of positive electrode plates were produced by drying.
(2)負極(負極板)の作製
鉛粉と、リグニンスルホン酸ナトリウム(有機防縮剤)と、カーボンブラックと、硫酸バリウムと、希硫酸とを混合して、負極ペーストを調製した。鉛粉100質量部に対して、リグニンスルホン酸ナトリウムを0.3質量部、カーボンブラック(導電剤)を0.4質量部、硫酸バリウムを0.5質量部用いた。調製した負極ペーストを、集電体の格子部に充填し、熟成させた。さらに乾燥させることによって、負極板を複数作製した。
(2) Production of negative electrode (negative electrode plate) Lead powder, sodium lignin sulfonate (organic anti-shrinkage agent), carbon black, barium sulfate, and dilute sulfuric acid were mixed to prepare a negative electrode paste. 0.3 parts by mass of sodium lignin sulfonate, 0.4 parts by mass of carbon black (conductive agent), and 0.5 parts by mass of barium sulfate were used with respect to 100 parts by mass of lead powder. The prepared negative electrode paste was filled in the grid portion of the current collector and aged. Further, a plurality of negative electrode plates were produced by drying.
(3)セパレータ
セパレータとして、厚さが1mmのPE製微多孔膜を用いた。
(3) Separator A PE microporous film with a thickness of 1 mm was used as a separator.
(4)孔あきシートの作製
孔あきシートの原反として、厚さが0.1mmのPP製不織布を用いた。表1に示す開口率となるように、打ち抜き加工によって複数の貫通孔(円形、直径約3.6mm、孔面積10mm2)を形成した。
(4) Production of perforated sheet A PP non-woven fabric having a thickness of 0.1 mm was used as the raw sheet of the perforated sheet. A plurality of through-holes (circular, diameter: about 3.6 mm, hole area: 10 mm 2 ) were formed by punching so as to achieve the aperture ratio shown in Table 1.
(5)電解液の調製
電解液として、密度(20℃)が1.280g/cm3の硫酸水溶液を調製した。
(5) Preparation of Electrolytic Solution As an electrolytic solution, an aqueous sulfuric acid solution having a density (20 ° C.) of 1.280 g / cm 3 was prepared.
(6)ケース内への極板群の配置
上記の正極板(6枚)、上記の負極板(7枚)、上記の電解液、上記のセパレータ、上記の孔あきシート、及び電槽(ケース)を用いて、常法に従って液式の鉛蓄電池を組み立てた。
まず、複数のセパレータが、上記の正極板及び負極板の間に配されて積層された極板群を作製した。このとき、孔あきシートを、負極板とセパレータとの間に配置した。次に、隔壁によって仕切られたケース本体の各セル室に、極板群を1つずつ収容した。複数の極板群を直列に接続し、ケース本体の開口を蓋部で塞いだ後、電槽の内部に電解液を入れ、電池を組み立てた。
(6) Arrangement of electrode plate group in case The positive electrode plate (six pieces), the negative electrode plate (seven pieces), the electrolytic solution, the separator, the perforated sheet, and the battery case (case) ) Was used to assemble a liquid lead-acid battery according to a conventional method.
First, an electrode plate group was prepared in which a plurality of separators were disposed between the positive electrode plate and the negative electrode plate and stacked. At this time, the perforated sheet was disposed between the negative electrode plate and the separator. Next, one electrode plate group was accommodated in each cell chamber of the case body partitioned by the partition walls. A plurality of electrode plate groups were connected in series, and the opening of the case body was closed with a lid, and then the electrolyte was put into the battery case to assemble the battery.
(7)化成処理
組み立てた電池に対して化成処理を施し、35Ahの鉛蓄電池を製造した。
(7) Chemical conversion treatment Chemical conversion treatment was applied to the assembled battery to produce a 35 Ah lead acid battery.
(試験例2~7)
表1に示すように、孔あきシートの開口率をそれぞれ変えた点、又は、孔あきシートを用いなかった点など以外は、試験例1と同様にして電池を製造した。
(Test Examples 2 to 7)
As shown in Table 1, a battery was manufactured in the same manner as in Test Example 1 except that the aperture ratio of the perforated sheet was changed or the perforated sheet was not used.
(試験例8~14)
表2に示すように、孔あきシートの開口率をそれぞれ変えた点、又は、孔あきシートを用いなかった点など以外は、試験例1と同様にして電池を製造した。
(Test Examples 8 to 14)
As shown in Table 2, a battery was manufactured in the same manner as in Test Example 1 except that the aperture ratio of the perforated sheet was changed or the perforated sheet was not used.
<繰り返し充放電に対する耐久性の評価試験(サイクル耐久性試験)>
各試験例の鉛蓄電池を用いて、繰り返し充放電に対する耐久性を評価した。表1における試験は、サイクルパターンI(放電1.25I5、 2h、充電1.25I5 5h、最大電圧2.7V/cell)で行なった。放電時の電池電圧が10.2Vになった時点で寿命と判定し、寿命となるまでの充放電サイクル数をもって繰り返し充放電に対する耐久性とした。一方、表2における試験は、サイクルパターンII(放電0.5I5、 2h、充電0.5I5 5h、最大電圧2.4V/cell)で行なった。放電時の電池電圧が10.2Vになった時点で寿命と判定し、寿命となるまでの充放電サイクル数をもって繰り返し充放電に対する耐久性とした。
繰り返し充放電に対する耐久性の評価試験の結果を、表1及び表2に示す。
<Durability evaluation test for repeated charge / discharge (cycle durability test)>
The durability against repeated charge and discharge was evaluated using the lead storage battery of each test example. The test in Table 1 was performed with cycle pattern I (discharge 1.25I 5 , 2h, charge 1.25I 5 5h, maximum voltage 2.7V / cell). When the battery voltage at the time of discharge became 10.2 V, it was determined as the life, and the number of charge / discharge cycles until the end of the life was determined as the durability against repeated charge / discharge. On the other hand, the test in Table 2 was performed with cycle pattern II (discharge 0.5I 5 , 2h, charge 0.5I 5 5h, maximum voltage 2.4V / cell). When the battery voltage at the time of discharge became 10.2 V, it was determined as the life, and the number of charge / discharge cycles until the end of the life was determined as the durability against repeated charge / discharge.
Tables 1 and 2 show the results of durability evaluation tests for repeated charge and discharge.
<電流分布の均一さの評価試験>
各試験例の鉛蓄電池を用いて、電流分布の均一程度を評価した。詳しくは、極板群が電解液に浸かった状態で、正極板及び負極板の下端に鉛線を接続し、上記の鉛線と同じ極性の端子間の電圧を測定することによって、電流分布の均一さを評価した。充放電中において、測定した電位差が常に一定である場合、電流分布は、ほぼ均一と考えられる。一方、電圧差が変動する場合、電流分布は、不均一になっている。孔あきシートを有しない鉛蓄電池を比較対象として、斯かる電池の極板電位差の変化幅に対して、極板電位差の変化幅が20%以上低下した試験例の電池をA、20%未満かつ10%以上低下した試験例の電池をB、10%未満しか低下しなかった試験例の電池をCと判定した。斯かる判定は、全充放電サイクルを通した極板電位差の変化幅の平均値を基にした。
電流分布の均一さの評価試験の結果を、表1及び表2に示す。また、斯かる評価試験において、電位差の測定結果の一例を経時的に示したグラフを図4に示す。
<Evaluation test of current distribution uniformity>
Using the lead storage battery of each test example, the degree of current distribution uniformity was evaluated. Specifically, in a state where the electrode plate group is immersed in the electrolytic solution, a lead wire is connected to the lower ends of the positive electrode plate and the negative electrode plate, and the voltage between the terminals having the same polarity as the above lead wire is measured. Uniformity was evaluated. If the measured potential difference is always constant during charging and discharging, the current distribution is considered to be substantially uniform. On the other hand, when the voltage difference fluctuates, the current distribution is not uniform. For a lead storage battery having no perforated sheet, the battery of the test example in which the change width of the electrode plate potential difference is reduced by 20% or more with respect to the change width of the electrode plate potential difference of such a battery is A, less than 20% and The battery of the test example that decreased by 10% or more was determined as B, and the battery of the test example that decreased by less than 10% was determined as C. Such a determination was based on the average value of the change width of the electrode plate potential difference through the entire charge / discharge cycle.
Tables 1 and 2 show the results of the evaluation test of the uniformity of the current distribution. FIG. 4 shows a graph showing an example of the measurement result of the potential difference over time in such an evaluation test.
上記の表1及び表2の結果を基にして、以下の考察を行なった。
一般的に、液式鉛蓄電池においては、放電深度の深い充電又は放電を実施すると、放電又は充電の各反応が、極板の上部又は下部のいずれかで偏って起こり、極板の上下方向において不均一に進行する。すなわち、極板における電流分布が不均一になる。そして、極板の劣化が生じ得る。なお、充放電反応における電流分布の不均一さは、電解液の成層化や格子体の集電性能などによって起こると考えられる。
これに対して、複数の貫通孔が形成された孔あきシート(例えば不織布)であって、上部と下部とで開口率が異なる孔あきシートを用いることによって、充放電における電流分布を均一に近づけられることがわかった。
不織布は、多孔質であり、電解液を含浸できることから、正極板及び負極板の間に不織布を配置しても、正極板及び負極板の間での充放電反応は、あまり抑制されずに進行する。換言すると、正極板及び負極板間における上記充放電反応は、孔が形成されていない部分(非貫通部分)を介しても進行する。また、貫通孔が形成されていることによって、上記充放電反応は、貫通孔を介して、より十分に進行すると考えられる。
充放電においては、一般的に、正極板と負極板との間に流れる電流は、必ずしも極板の同じ高さ部分同士の間で流れるわけではなく、異なる高さ部分の間でも流れる。具体的には、放電初期においては、負極上部に向かって電流が集中するように流れ、充電初期においては、負極下部に向かって電流が集中するように流れる傾向にある。よって、充放電電流は、上方向又は下方向のいずれかの方へ偏って流れる。そこで、開口率が上部と下部で異なる貫通孔を有する孔あきシートを用いることによって、極板間における電流の上下方向の流れ、すなわち電解液中のイオンの上下方向での移動を、開口率が高い方よりも低い方において、制限することができる。充放電反応が起こりやすい方(例えば電解液の上部又は下部のいずれか)に、孔あきシートの開口率が低い方(孔あきシートの上部又は下部のいずれか)を配置することによって、充放電電流の偏りを均一に近づけることができる。これにより、正極板と負極板とにおける同じ高さ部分同士の経路での充放電反応を起こりやすくできると考えられる。
一方、開口率が上部と下部で等しい貫通孔を有する孔あきシートを用いた場合、上部と下部とにおいて、電解液中のイオンの上下方向での移動が必ずしも制限されないため、電流分布の不均一さを解消できないと考えられる。
Based on the results shown in Tables 1 and 2, the following considerations were made.
In general, in a liquid lead-acid battery, when charging or discharging at a deep discharge depth is performed, each reaction of discharging or charging occurs unevenly in either the upper part or the lower part of the electrode plate, and in the vertical direction of the electrode plate. Proceeds unevenly. That is, the current distribution in the electrode plate becomes non-uniform. And deterioration of an electrode plate may arise. In addition, the non-uniformity of the current distribution in the charge / discharge reaction is considered to occur due to the stratification of the electrolytic solution, the current collecting performance of the lattice, and the like.
On the other hand, by using a perforated sheet (for example, a non-woven fabric) in which a plurality of through-holes are formed and having different opening ratios between the upper part and the lower part, the current distribution in charge and discharge is made closer to uniform. I found out that
Since the nonwoven fabric is porous and can be impregnated with an electrolytic solution, even if the nonwoven fabric is disposed between the positive electrode plate and the negative electrode plate, the charge / discharge reaction between the positive electrode plate and the negative electrode plate proceeds without being suppressed so much. In other words, the charge / discharge reaction between the positive electrode plate and the negative electrode plate proceeds even through a portion where a hole is not formed (non-penetrating portion). Moreover, it is considered that the charge / discharge reaction proceeds more sufficiently through the through-hole by forming the through-hole.
In charging / discharging, generally, the current flowing between the positive electrode plate and the negative electrode plate does not necessarily flow between the same height portions of the electrode plates, but also flows between different height portions. Specifically, in the initial stage of discharge, the current tends to concentrate toward the upper part of the negative electrode, and in the initial stage of charging, the current tends to flow toward the lower part of the negative electrode. Therefore, the charge / discharge current flows in a biased direction either upward or downward. Therefore, by using a perforated sheet having through holes with different opening ratios at the top and bottom, the flow of current between the plates in the vertical direction, that is, the movement of ions in the electrolyte in the vertical direction, It can be limited on the lower side than the higher side. Charging / discharging by placing the one with a lower aperture ratio of the perforated sheet (either the upper part or the lower part of the perforated sheet) on the one where charge / discharge reaction is likely to occur (for example, either the upper part or the lower part of the electrolyte) The current bias can be made uniform. Thereby, it is thought that the charging / discharging reaction in the path | route of the same height part in a positive electrode plate and a negative electrode plate can occur easily.
On the other hand, when a perforated sheet having through-holes with the same opening ratio at the upper and lower portions is used, the vertical movement of ions in the electrolyte solution is not necessarily restricted between the upper and lower portions, so that the current distribution is uneven. It is thought that this cannot be resolved.
例えば、孔あきシートの開口率が上部で高くかつ下部で低い場合には、上部よりも下部において、電解液中のイオンの上下方向での移動が制限される。その結果、負極板の上部に向かって電流が集中するとき(例えば放電時)に、正極板の下部から負極板の上部に向かう電流を抑制できる。従って、電流分布を均一に近づけることができると考えられる。
一方で、例えば、孔あきシートの開孔率が下部で高くかつ上部で低い場合には、下部よりも上部において電解液中のイオンの上下方向での移動が制限される。その結果、負極板の下部に向かって電流が集中するとき(例えば充電時)に、正極板の上部から負極板の下部に向かう電流を抑制できる。従って、電流分布を均一に近づけることができると考えられる。
これに加え、不織布の非貫通部分を介して互いに向き合う正極活物質と負極活物質との間での充放電反応は、貫通孔を介することによって、進行しやすくなると考えられる。詳しくは、一方の極板の活物質と他方の極板の活物質とが同じ高さ位置にあり、かつ、これら活物質の間に非貫通部分があったとしても、一方の活物質と他方の活物質との間で、貫通孔を介して、例えば迂回するような経路で、反応が進行する。また、互いに異なる高さ位置にある一方の活物質と他方の活物質との間に貫通孔があると、貫通孔を介して、例えば上下に傾斜したような経路で、反応が進行する。このように、貫通孔の存在によって、正極板及び負極板の間における充放電反応が、同じ高さ間の経路で進行するだけでなく、異なる高さ間の経路でも進行しやすくなると考えられる。よって、不均一になりやすい上下方向での電流分布を、均一に近づけることができ、サイクル耐久性が向上すると考えられる。
For example, when the aperture ratio of the perforated sheet is high at the top and low at the bottom, the movement of ions in the electrolyte in the vertical direction is restricted at the bottom rather than the top. As a result, when the current concentrates toward the upper part of the negative electrode plate (for example, during discharge), the current flowing from the lower part of the positive electrode plate to the upper part of the negative electrode plate can be suppressed. Therefore, it is considered that the current distribution can be made close to uniform.
On the other hand, for example, when the aperture ratio of the perforated sheet is high at the lower part and low at the upper part, the movement of ions in the electrolytic solution in the upper and lower direction is restricted above the lower part. As a result, when the current concentrates toward the lower part of the negative electrode plate (for example, during charging), the current flowing from the upper part of the positive electrode plate to the lower part of the negative electrode plate can be suppressed. Therefore, it is considered that the current distribution can be made close to uniform.
In addition to this, it is considered that the charge / discharge reaction between the positive electrode active material and the negative electrode active material facing each other through the non-penetrating portion of the nonwoven fabric easily proceeds by way of the through hole. Specifically, even if the active material of one electrode plate and the active material of the other electrode plate are at the same height position and there is a non-penetrating part between these active materials, The reaction proceeds with the active material through a through hole, for example, in a detour path. In addition, when there is a through hole between one active material and the other active material at different height positions, the reaction proceeds through a through hole, for example, along a path inclined upward and downward. Thus, it is considered that the presence / absence of the through-hole facilitates the charge / discharge reaction between the positive electrode plate and the negative electrode plate not only in the path between the same height but also in the path between the different heights. Therefore, it is considered that the current distribution in the vertical direction, which tends to be non-uniform, can be made closer to uniform and cycle durability is improved.
また、表1及び表2から把握されるように、孔あきシートの上部の開口率(%)と下部の開口率(%)との差が15ポイント以上であることによって、上部の開口率が高い場合には、特に放電において充放電分布を均一に近づけられる(表1)。一方、下部の開口率が高い場合には、特に充電において充放電分布を均一に近づけられる(表2)。 Further, as understood from Table 1 and Table 2, the difference between the opening ratio (%) of the upper part of the perforated sheet and the opening ratio (%) of the lower part is 15 points or more, so that the opening ratio of the upper part is When it is high, the charge / discharge distribution can be made uniform even in the discharge (Table 1). On the other hand, when the opening ratio at the lower part is high, the charge / discharge distribution can be made uniform even in charging (Table 2).
(試験例15~17)
表3に示すように、孔あきシートの貫通孔の孔面積(1つあたり)をそれぞれ変えた点、又は、孔あきシートを用いなかった点など以外は、試験例1と同様にして電池を製造した。
(Test Examples 15 to 17)
As shown in Table 3, the battery was fabricated in the same manner as in Test Example 1 except that the hole area (per one) of the through holes of the perforated sheet was changed or the perforated sheet was not used. Manufactured.
<繰り返し充放電後の電解液の比重差の評価試験>
サイクルパターンIの条件で充放電サイクルを20回行った後に、電解液の上部及び下部からサンプルを採取して、電解液の比重を測定した。電解液の比重の測定方法は、光学式比重計などの公知の方法を用いることができる。
<Evaluation test of difference in specific gravity of electrolyte after repeated charge and discharge>
After 20 charge / discharge cycles were performed under the conditions of cycle pattern I, samples were taken from the upper and lower portions of the electrolytic solution, and the specific gravity of the electrolytic solution was measured. As a method for measuring the specific gravity of the electrolytic solution, a known method such as an optical hydrometer can be used.
表3から把握されるように、貫通孔が形成され、かつ、開口率が上部と下部とで異なる孔あきシートを正極板と負極板との間に配置することによって、電解液の成層化を抑制できる(特に、試験例16)。
詳しくは、開口率が上部と下部とで異なる孔あきシートを用いることによって、上述したように電流分布を均一に近づけることができると考えられる。これにより、電解液の上下方向における濃度差を抑えることができ、成層化を抑制できたと考えられる。成層化が抑制されることにより、繰り返し充放電に対する耐久性を向上できると考えられる。
また、孔あきシートの貫通孔の大きさが10mm2以上であることによって、充放電反応に伴って発生するガスが孔を閉塞することをより抑制できる。よって、充放電反応における電気的経路を確保できる。成層化がすでに起こっていても、極板の下部における充電ガスを発生させやすくでき、成層化を解消することが促進される。一方、貫通孔の大きさが200mm2よりも小さいことによって、同じ高さにおける充放電特性の差をより小さくでき、寿命性能の悪化を抑制できる。
As can be seen from Table 3, the electrolyte solution is stratified by arranging a perforated sheet in which through holes are formed and the opening ratios are different between the upper part and the lower part between the positive electrode plate and the negative electrode plate. (In particular, Test Example 16).
Specifically, it is considered that the current distribution can be made closer to uniform as described above by using perforated sheets having different opening ratios at the upper part and the lower part. Thereby, the concentration difference in the vertical direction of the electrolytic solution can be suppressed, and it is considered that stratification can be suppressed. It is considered that durability against repeated charge / discharge can be improved by suppressing stratification.
Moreover, it can suppress more that the gas generate | occur | produced with charging / discharging reaction obstruct | occludes a hole because the magnitude | size of the through-hole of a perforated sheet | seat is 10 mm < 2 > or more. Therefore, the electrical path | route in charging / discharging reaction is securable. Even if stratification has already occurred, it is easy to generate charging gas in the lower part of the electrode plate, and it is promoted to eliminate stratification. On the other hand, when the size of the through hole is smaller than 200 mm 2 , the difference in charge / discharge characteristics at the same height can be further reduced, and deterioration of the life performance can be suppressed.
下記の表4に、試験例1の孔あきシートの配置を変えた鉛蓄電池を用いて、上記と同様にして、繰り返し充放電に対する耐久性を評価した結果を示す(試験例1’)。詳しくは、正極板と負極板に配置された孔あきシートが、セパレータよりも負極板側に配置された場合(負極側)と、セパレータよりも正極板側に配置された場合(正極側)と、における結果を表4に示す。
表4から把握されるように、孔あきシートを負極側に配置することによって、繰り返し充放電に対する耐久性を、より向上させることができる。
Table 4 below shows the results of evaluating the durability against repeated charge and discharge in the same manner as described above using the lead storage battery in which the arrangement of the perforated sheet of Test Example 1 was changed (Test Example 1 ′). Specifically, when the perforated sheets arranged on the positive electrode plate and the negative electrode plate are arranged on the negative electrode plate side with respect to the separator (negative electrode side), and on the positive electrode plate side with respect to the separator (positive electrode side) Table 4 shows the results.
As can be seen from Table 4, by disposing the perforated sheet on the negative electrode side, durability against repeated charge / discharge can be further improved.
1:鉛蓄電池、
10:極板群、
20:正極板(正極)、 21:正極集電体、 22:正極電極材料、
30:負極板(負極)、 31:負極集電体、 32:負極電極材料、
40:セパレータ、 50:孔あきシート、 A:貫通孔、
60:電槽(ケース)、 61:ケース本体、 62:蓋部、
70:正極端子、 71:正極用ストラップ、
80:負極端子、 81:負極用ストラップ、
90:接続部材、 91:液口栓。
1: lead acid battery,
10: Electrode plate group,
20: positive electrode plate (positive electrode), 21: positive electrode current collector, 22: positive electrode material,
30: Negative electrode plate (negative electrode), 31: Negative electrode current collector, 32: Negative electrode material,
40: Separator, 50: Perforated sheet, A: Through hole,
60: Battery case (case), 61: Case body, 62: Cover part,
70: positive electrode terminal, 71: strap for positive electrode,
80: negative electrode terminal, 81: strap for negative electrode,
90: connecting member, 91: liquid spout.
Claims (6)
前記孔あきシートにおける開口率は、上部と下部とで異なる、鉛蓄電池。 A positive electrode plate, a negative electrode plate, a perforated sheet disposed between the positive electrode plate and the negative electrode plate and having a through-hole formed in a thickness direction, and an electrolyte solution,
The lead storage battery in which the aperture ratio in the perforated sheet is different between the upper part and the lower part.
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| CN201980034079.0A CN112154555A (en) | 2018-05-23 | 2019-05-14 | Lead-acid battery |
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| KR20240044427A (en) | 2021-08-24 | 2024-04-04 | 엔텍 아시아 가부시키가이샤 | Pasting paper for lead acid batteries |
| JP2025009397A (en) * | 2023-07-07 | 2025-01-20 | プライムプラネットエナジー&ソリューションズ株式会社 | Secondary battery |
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| JPH06187967A (en) * | 1992-10-13 | 1994-07-08 | Yuasa Corp | Clad type sealed lead-acid battery |
| JP2002216838A (en) * | 2001-01-19 | 2002-08-02 | Yuasa Corp | Control valve type lead storage battery |
| JP2002222654A (en) * | 2001-01-26 | 2002-08-09 | Matsushita Electric Ind Co Ltd | Current collector for battery, and battery and lead storage battery having the same |
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| JP2017068920A (en) * | 2015-09-28 | 2017-04-06 | 日立化成株式会社 | Lead storage battery |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH06187967A (en) * | 1992-10-13 | 1994-07-08 | Yuasa Corp | Clad type sealed lead-acid battery |
| JP2002216838A (en) * | 2001-01-19 | 2002-08-02 | Yuasa Corp | Control valve type lead storage battery |
| JP2002222654A (en) * | 2001-01-26 | 2002-08-09 | Matsushita Electric Ind Co Ltd | Current collector for battery, and battery and lead storage battery having the same |
Cited By (2)
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| KR20240044427A (en) | 2021-08-24 | 2024-04-04 | 엔텍 아시아 가부시키가이샤 | Pasting paper for lead acid batteries |
| JP2025009397A (en) * | 2023-07-07 | 2025-01-20 | プライムプラネットエナジー&ソリューションズ株式会社 | Secondary battery |
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| JP7352870B2 (en) | 2023-09-29 |
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