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AU2016200589B2 - Lead-acid battery - Google Patents
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AU2016200589B2 - Lead-acid battery - Google Patents

Lead-acid battery Download PDF

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AU2016200589B2
AU2016200589B2 AU2016200589A AU2016200589A AU2016200589B2 AU 2016200589 B2 AU2016200589 B2 AU 2016200589B2 AU 2016200589 A AU2016200589 A AU 2016200589A AU 2016200589 A AU2016200589 A AU 2016200589A AU 2016200589 B2 AU2016200589 B2 AU 2016200589B2
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Prior art keywords
graphite
mass
lead
negative electrode
active material
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AU2016200589A1 (en
Inventor
Satoshi Inagaki
Masaaki Kyo
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GS Yuasa International Ltd
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GS Yuasa International Ltd
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    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/62Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
    • H01M4/624Electric conductive fillers
    • H01M4/625Carbon or graphite
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M10/00Secondary cells; Manufacture thereof
    • H01M10/06Lead-acid accumulators
    • H01M10/12Construction or manufacture
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/02Electrodes composed of, or comprising, active material
    • H01M4/14Electrodes for lead-acid accumulators
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M2220/00Batteries for particular applications
    • H01M2220/20Batteries in motive systems, e.g. vehicle, ship, plane
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50Manufacturing or production processes characterised by the final manufactured product

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Battery Electrode And Active Subsutance (AREA)
  • Secondary Cells (AREA)

Abstract

OF THE DISCLOSURE A lead-acid battery includes a negative electrode material containing graphite or carbon fiber. The ratio of the mass of the negative electrode material to the mass of a positive electrode material is 0.62 or more. [1/4] FIG. 1 16 18 16 16 1 14:> FIG. 2 A~ x50time 1cycle ..... tDisharg,N ...... I 5times

Description

[1/4]
FIG. 1
16 18 16 16
1
14:>
FIG. 2
A~ x50time 1cycle .....
tDisharg,N ......
I 5times
LEAD-ACID BATTERY FIELD
The present invention relates to a lead-acid battery, and particularly
relates to a lead-acid battery which is used in an environment involving deep
discharge.
BACKGROUND
With the advent of idling-stop vehicles, lead-acid batteries have been
deeply discharged more often than before. For example, lead-acid batteries
of idling-stop vehicles are based on the premise that they are used in a
partial state of charge (PSOC). Lead-acid batteries for cycle applications
like those for forklift trucks have been used at a deep depth of discharge
(DOD). When a lead-acid battery is used in a partial state of charge, its life
is reduced due to accumulation of lead sulfate in a positive electrode or
sulfation of a negative electrode. In the partial state of charge, agitation of
an electrolyte solution by gas evolution is insufficient, and thus the
electrolyte solution is easily stratified. This further reduces the life of a
lead-acid battery.
Meanwhile, when the lead-acid battery transitions into an
overdischarged state from the partial state of charge because, for example,
the vehicle is left unattended for a long period of time, metal lead passes
through the separator, and thus a permeation short circuit, in which both
positive and negative electrode plates are short-circuited, easily occurs.
The concentration of sulfate ions in the electrolyte solution decreases due to
overdischarge, and correspondingly, the concentration of lead ions in the
electrolyte solution increases. The lead ions are reduced on the negative electrode plate during charge, and metal lead dendrite grows through pores inside the separator, and thus passes through the separator to short-circuit the positive electrode plate and the negative electrode plate.
The applicant proposed improvement of the life of a lead-acid battery
in the PSOC by including graphite in a negative electrode material. For
example, Patent Document 1 (WO 2011/90113) discloses that a negative
electrode material is made to contain 0.02 to 2.20 mass% of graphite, 0.5
mass% of barium sulfate, and 0.02 to 2.20 mass% of carbon black. Patent
Document 2 (WO 2011/52438) discloses that a negative electrode material is
made to contain 0.5 to 3.0 mass% of expanded graphite and 0.6 mass% of
barium sulfate. Among documents other than those by the applicant, for
example, Patent Document 3 (JP5584216 B) discloses that a negative
electrode material is made to contain 1 to 3 mass% of graphite, 0.8 mass% of
barium sulfate, and 0.1 to 2 mass% of carbon black.
Patent Document 4 (JP5596241 B) discloses that a mass ratio MN/MP
is in a range of from 0.70 to 1.10 where Mp is the mass of the positive active
material, and MN is the mass of the negative active material, per cell
chamber.
SUMMARY
Graphite particles form a path for electrons to lead sulfate, and thus
facilitate charge at a negative electrode. The inventors have found, in the
process of conducting studies on improvement of the PSOC life, that graphite
in a negative electrode material causes a permeation short circuit. This can
be because when a graphite particle is exposed to, or protrudes from, a
surface of a negative electrode plate, the exposed portion or the like of the
graphite particle serves as a center of precipitation of metal lead. As a result, metal lead dendrite may grow from an exposed graphite particle, and then pass through the separator to cause a short circuit. The fact that graphite in the negative electrode material causes a permeation short circuit was not known, and was first found by the present inventors. The present inventors have also found that, when the negative electrode material contains carbon fiber, the carbon fiber in the negative electrode material causes a permeation short circuit, similarly.
An object of the present invention is to provide a lead-acid battery
that is:
• unlikely to be subjected to a permeation short circuit caused by
graphite or carbon fiber, and
• excellent in life performance in an environment involving deep
discharge, such as a PSOC.
An aspect of the present invention provides a lead-acid battery
including a negative electrode plate, a positive electrode plate, and an
electrolyte solution, wherein the negative electrode plate includes a negative
electrode material containing graphite or carbon fiber, and a ratio N/P
(hereinafter referred to as "N/P ratio") of a mass N of the negative electrode
material to a mass P of the positive electrode material, per lead-acid battery,
is 0.62 or more.
BRIEF DESCRIPTION OF DRAWINGS
Fig. 1 is a sectional view of a part of a lead-acid battery in an
example.
Fig. 2 is a diagram showing a PSOC life test in the example.
Fig. 3 is a characteristic diagram showing the influence of the
content of graphite (content of barium sulfate: 0.6 mass%, N/P ratio: 0.95).
Fig. 4 is a characteristic diagram showing the influence of the N/P
ratio (content of barium sulfate: 0.6 mass%).
Fig. 5 is a characteristic diagram showing the influence of the N/P
ratio (content of barium sulfate: 0.6 mass%).
Fig. 6 is a characteristic diagram showing the influence of the
content of barium sulfate (content of graphite: 0.5 mass%, N/P ratio: 0.62).
Fig. 7 is a characteristic diagram showing the influence of the
average particle size of graphite (content of graphite: 2.0 mass%, content of
barium sulfate: 1.2 mass%, N/P ratio: 0.78).
Fig. 8 is a characteristic diagram showing the influence of the
content of carbon black (content of graphite: 2.0 mass%, content of barium
sulfate: 1.2 mass%, N/P ratio: 0.62).
Fig. 9 is a characteristic diagram showing the influence of the
concentration of aluminum ions (content of graphite: 2.0 mass%, content of
barium sulfate: 1.2 mass%, N/P ratio: 0.62).
Fig. 10 is a characteristic diagram showing the influence of the
concentration of lithium ions (content of graphite: 2.0 mass%, content of
barium sulfate: 1.2 mass%, N/P ratio: 0.62).
DESCRIPTION OF EMBODIMENTS
An aspect of the present invention provides a lead-acid battery
including a negative electrode plate, a positive electrode plate, and an
electrolyte solution, wherein the negative electrode plate includes a negative
electrode material containing graphite or carbon fiber, and a ratio N/P
(hereinafter referred to as "N/P ratio") of a mass N of the negative electrode
material to a mass P of the positive electrode material, per lead-acid battery,
is 0.62 or more.
The graphite may not only be scalelike graphite or expanded graphite
of Example, but may also be natural graphite such as scaly graphite or
earthy graphite, or artificial graphite, or expansion graphite, etc. Scalelike
graphite and expanded graphite are preferable, with scalelike graphite being
particularly preferable. Expanded graphite is graphite that has been
expanded. Carbon fiber has an effect similar to that of graphite. Carbon
fiber to be used has, for example, a length in a range of 5 im or more and 500
im or less.
Graphite or carbon fiber (hereinafter referred to as "graphite or the
like") in the negative electrode material facilitates reduction of lead sulfate
deposited on a lower portion of a plate of a lead-acid battery, and thus
improves life performance in a non-fully charged condition of the lead-acid
battery, such as a PSOC life. A content of graphite or the like in the
negative electrode material of 0.5 mass% or more significantly improves the
PSOC life, and is thus preferred. On the other hand, it has been found that
inclusion of graphite or the like in the negative electrode material causes a
permeation short circuit to easily occur. It was not known that inclusion of
graphite or the like in the negative electrode material of a lead-acid battery
causes a permeation short circuit to easily occur.
Thus, the present inventors conducted studies on inhibition of
occurrence of a permeation short circuit while graphite or the like is included
in the negative electrode material to improve the PSOC life. As a result, it
has been found that even when the negative electrode material contains
graphite or the like, an N/P ratio of 0.62 or more can inhibit a permeation
short circuit.
Inclusion of graphite or the like in the negative electrode material,
and an N/P ratio in a range of 0.62 or more and 0.95 or less significantly improves the PSOC life, and thus the N/P ratio is preferably in a range of
0.62 or more and 0.95 or less. An N/P ratio in a range of 0.62 or more and
0.78 or less more significantly improves the PSOC life, and thus the N/P
ratio is more preferably in a range of 0.62 or more and 0.78 or less.
A content of graphite or the like in the negative electrode material of
2.5 mass% or less can inhibit a permeation short circuit, and is thus
preferred. A content of graphite or the like in the negative electrode
material of 2.0 mass% or less can further inhibit a permeation short circuit,
and is thus more preferred.
Inclusion of barium sulfate in the negative electrode material can
inhibit a permeation short circuit, and is thus preferred. Inclusion of 1.2
mass% or more of barium sulfate in the negative electrode material can
markedly inhibit a permeation short circuit, and is thus more preferred.
Note that elemental barium or a barium compound such as barium
carbonate may be used instead of barium sulfate. This is because elemental
barium or a barium compound added to the negative electrode material
changes to barium sulfate after the addition. Elemental barium or a
barium compound is preferably added in an amount equivalent to 1.2 mass%
or more of barium sulfate with respect to the mass of the negative electrode
material in a fully-charged state. In terms of content equivalent to
elemental barium, the addition is preferably performed so that the content of
barium in the negative electrode material will be 0.7 mass% or more.
Inclusion of more than 3.0 mass% of barium sulfate in the negative
electrode material markedly reduces the PSOC life. This cancels the effect
of improving the PSOC life produced by inclusion of graphite or the like in
the negative electrode material. Thus, the content of barium sulfate in the
negative electrode material is preferably 3.0 mass% or less. In terms of content equivalent to elemental barium, the addition is preferably performed so that the content of barium in the negative electrode material will be 1.75 mass% or less.
Inclusion of 2.5 mass% or less of graphite or the like in the negative
electrode material, inclusion of 1.2 mass% or more of barium sulfate in the
negative electrode material, and an N/P ratio of 0.62 or more can yield a
lead-acid battery having excellent PSOC life performance and excellent
permeation short circuit resistance performance, and are thus preferred.
Inclusion of 2.0% or less of graphite or the like in the negative electrode
material, inclusion of 1.2 mass% or more of barium sulfate in the negative
electrode material, and an N/P ratio of 0.62 or more can yield a lead-acid
battery having particularly excellent permeation short circuit resistance
performance, and are thus more preferred.
Even when the negative electrode material contains 2.5 mass% or
less of graphite or the like, the negative electrode material contains 1.2
mass% or more of barium sulfate, and the N/P ratio is 0.62 or more, a
permeation short circuit may not be completely prevented. Thus, the
present inventors have conducted studies on further inhibiting a permeation
short circuit.
An average particle size of graphite in the negative electrode
material of 300 pm or less can further inhibit a permeation short circuit, and
therefore, the average particle size of graphite in the negative electrode
material is preferably 300 pm or less.
An average particle size of graphite in the negative electrode
material of 10 pm or more improves the PSOC life, and thus the average
particle size of graphite in the negative electrode material is preferably 10
pm or more.
Preferably, the negative electrode material contains carbon black.
By including carbon black in the negative electrode material, an effect of
further inhibiting a permeation short circuit is obtained. The effect of
carbon black of inhibiting a permeation short circuit is noticeable when the
content of carbon black in the negative electrode material is 0.05 mass% or
more, and thus the content of carbon black in the negative electrode material
is preferably 0.05 mass% or more.
A content of carbon black in the negative electrode material of 0.1
mass% or more produces a larger effect of improving the PSOC life than
when the content of carbon black in the negative electrode material is less
than 0.1 mass%. Thus, the content of carbon black in the negative electrode
material is preferably 0.1 mass% or more. A content of carbon black in the
negative electrode material of 0.5 mass% or more produces an especially
large effect of improving the PSOC life. Therefore, the content of carbon
black in the negative active material is more preferably 0.5 mass% or more.
A content of carbon black in the negative electrode material of more than 1.0
mass% causes the negative active material paste to be too hard to fill the
current collector. Therefore, the content of carbon black in the negative
electrode material is preferably 1.0 mass% or less.
Inclusion of aluminum ions in the electrolyte solution improves the
PSOC life. Inclusion of 0.02 mol/L or more of aluminum ions in the
electrolyte solution significantly improves the PSOC life. Thus, the
concentration of aluminum ions in the electrolyte solution is preferably 0.02
mol/L or more. Inclusion of 0.2 mol/L or less of aluminum ions in the
electrolyte solution significantly improves the PSOC life. Thus, the
concentration of aluminum ions in the electrolyte solution is preferably 0.2
mol/L or less.
Inclusion of lithium ions in the electrolyte solution can further
inhibit a permeation short circuit. This effect is significant when the
electrolyte solution contains 0.02 mol/L or more of lithium ions. Thus, the
concentration of lithium ions in the electrolyte solution is preferably 0.02
mol/L or more.
Inclusion of 0.1 mol/L or more of lithium ions in the electrolyte
solution improves the PSOC life. Thus, the concentration of lithium ions in
the electrolyte solution is preferably 0.1 mol/L or more. Moreover, inclusion
of 0.2 mol/L or less of lithium ions in the electrolyte solution improves the
PSOC life. Thus, the concentration of lithium ions in the electrolyte
solution is preferably 0.2 mol/L or less.
Most preferably, the electrolyte solution contains aluminum ions and
lithium ions.
The lead-acid battery of the present invention has excellent PSOC
life performance and excellent permeation short circuit resistance
performance, and is thus suitable as a lead-acid battery, such as for use in an
idling-stop vehicle. The lead-acid battery of the present invention can be
used not only for idling-stop vehicles etc., but also for cycle applications of,
for example, forklift trucks. In Example, the lead-acid battery is a
flooded-type lead-acid battery, but may also be a valve-regulated lead-acid
battery. The lead-acid battery of the present invention is preferably a
flooded-type lead-acid battery. The lead-acid battery of the present
invention is less likely to cause a permeation short circuit even when it is
used in a partial state of charge, and therefore, is suitable as a lead-acid
battery to be used in a partial state of charge.
The best mode example according to the invention of the present
application will be shown below. In embodying the present invention, the example can be appropriately changed based on common knowledge of a person skilled in the art and on disclosures of prior arts. In the example, the negative electrode material is also referred to as a negative active material, and the positive electrode material is also referred to as a positive active material. The negative electrode plate includes a negative electrode current collector (negative electrode grid) and a negative active material
(negative electrode material), and the positive electrode plate includes a
positive electrode current collector (positive electrode grid) and a positive
active material (positive electrode material). Solid components other than
the current collectors belong to the active materials (electrode materials).
[Example]
The negative active material paste was produced by mixing a
predetermined amount of graphite, a predetermined amount of barium
sulfate, lignin as a shrink-proofing agent, and synthetic resin fibers as a
reinforcing material with a lead powder produced by a ball milling method.
Carbon black was further included in the resultant mixture to prepare
another negative active material paste. Hereinafter, a content is expressed
in a concentration (mass%) in a formed negative active material after full
charge. The term "full charge" refers to a state in which charge has been
performed at a 5-hour rate current until the terminal voltage during charge
as measured every 15 minutes exhibits a particular value (0.01 V) three
times in succession.
The content of graphite was changed in a range of from 0 to 3.0
mass% with respect to the mass of the negative active material in a
fully-charged condition. Although scalelike graphite and expanded
graphite were used as graphite, other graphite such as earthy graphite and
artificial graphite, and carbon fiber may also be used. Both graphite and carbon fiber have high electrical conductivities, and are composed of particles larger than those of carbon black or the like. Actions thereof in the negative active material are also considered similar to each other. Among graphite and carbon fiber, scalelike graphite or expanded graphite is preferred. In particular, scalelike graphite or expanded graphite having an average particle size in a range of 10 pm or more and 300 pm or less is preferred. The scalelike graphite and expanded graphite used had resistivities as measured by a four-terminal method in a range of from 0.001
Q-cm to 0.01 Q-cm (resistivities under pressure of 2.5 MPa).
The content of barium sulfate was changed in a range of from 0.6
mass% to 4.0 mass% with respect to the mass of the negative active material
in a fully-charged condition. The barium sulfate used had an oil absorption
capacity of 12.5 mL/100 g, an average primary particle size of 0.79 pm, and
an average secondary particle size of 2.5 pm. However, properties of barium
sulfate, such as the particle sizes, the oil absorption capacity, etc. are not
limited. Barium sulfate has an average primary particle size of, for
example, 0.3 pm or more and 2.0 pm or less, and an average secondary
particle size of, for example, 1.0 pm or more and 10 pm or less. While the
content of lignin was 0.2 mass%, the content is not limited. A synthetic
shrink-proofing agent such as a condensate of a sulfonated bisphenol may be
used in place of lignin. While the content of the reinforcing material was
0.1 mass%, the content and the type of the synthetic resin fibers are not
limited. The method for producing a lead powder, the content of oxygen,
and so on are not limited. Other additives such as a water-soluble synthetic
polymer may be contained.
The above-mentioned mixture was formed into a paste with water
and sulfuric acid. An expanded type of negative electrode grid (110 mm
(height) x 100 mm (width) x 1.0 mm (thickness)) primarily composed of an
antimony-free Pb-Ca-Sn-based alloy was filled with this paste, which was
then cured and dried. The negative electrode grid may also be a cast grid, a
punched grid, or the like. The mass of the negative active material of each
negative electrode plate was made the same by dividing the mass of the
negative active material per cell shown in Tables 3 to 6 by the number of
negative electrode plates. In addition, the mass of the negative active
material per cell was made the same for all the cells. The density of the
negative active material after formation is in a range of, for example, 3.6
g/cm3 or more and 4.0 g/cm 3 or less. The amount of the filling negative active material per one negative electrode plate is in a range of, for example,
30 g or more and 70 g or less.
Synthetic resin fibers of a reinforcing material in an amount of 0.1
mass% with respect to the mass of the formed positive active material in a
fully-charged condition were mixed with a lead powder produced by a ball
milling method, and the resulting mixture was formed into a paste with
water and sulfuric acid, and was used as the positive active material paste.
An expanded type of positive electrode grid (110 mm (height) x 100 mm
(width) x 1.2 mm (thickness)) primarily composed of an antimony-free
Pb-Ca-Sn-based alloy was filled with this paste, which was then cured and
dried. The type of the lead powder and production conditions are not
limited. The grid may also be a cast grid, a punched grid, or the like. The
composition (components other than lead dioxide) of the positive active
material is not limited. For example, the positive active material may
contain antimony. The mass of the positive active material of each positive
electrode plate was made the same by dividing the mass of the positive active
material per cell shown in Tables 3 to 6 by the number of positive electrode plates. In addition, the mass of the positive active material per cell was made the same for all the cells. The density of the positive active material after formation is in a range of, for example, 3.5 g/cm 3 or more and 4.8 g/cm 3 or less.
An unformed negative electrode plate was wrapped with a
polyethylene separator with ribs protruding from a base, and seven
unformed negative electrode plates and six unformed positive electrode
plates were alternately layered. The negative electrode plates and the
positive electrode plates were connected to one another with a strap to
prepare an element. The separator is primarily composed of, for example, a
synthetic resin. The thickness of the base, the total thickness, and the like
are not limited. The thickness of the base of the separator was 0.25 mm,
but may be in a range of, for example, 0.15 mm or more and 0.25 mm or less.
The interval between a positive electrode plate and a negative electrode plate
is in a range of, for example, 0.5mm or more and 0.9mm or less. Six
elements connected in series were placed in a cell chamber of a container,
and sulfuric acid with a specific gravity of 1.230 at 20°C was added to
perform formation in the container, thereby preparing a flooded-type
lead-acid battery having a B20 size and a 5-hour rate capacity of 30 Ah.
Fig. 1 shows a part of a lead-acid battery 2. Reference numeral 4
denotes a negative electrode plate, reference numeral 6 denotes a positive
electrode plate, reference numeral 8 denotes a separator, and reference
numeral 10 denotes an electrolyte solution mainly composed of sulfuric acid.
The negative electrode plate 4 includes a negative electrode grid 12 and a
negative active material 14. The positive electrode plate 6 includes a
positive electrode grid 16 and a positive active material 18. The separator 8
is in the form of a bag including a base 20 and ribs 22. The negative electrode plate 4 is stored in the bag, and the ribs 22 face the positive electrode plate 6 side. However, the positive electrode plate 6 may be stored in the separator 8 with the ribs 22 facing the positive electrode plate. The separator is not required to be in the form of a bag as long as it isolates the positive electrode plate and the negative electrode plate from each other; the separator may be, for example, a leaflet-like glass mat or retainer mat.
The mass of the positive active material and the mass of the negative
active material, of the lead-acid battery 2, are determined as follows. The
lead-acid battery 2 in a fully-charged condition is disassembled, and the
negative electrode plate 4 is washed with water, and then dried, to remove
the sulfuric acid component. Thus, the negative active material 14 is
collected, and the mass of the negative active material per one negative
electrode plate is measured. In a similar manner, the positive active
material 18 is collected, and the mass of the positive active material per one
positive electrode plate is measured. The ratio of the sum of the mass of the
active material of all the negative electrode plates to the sum of the mass of
the active material of all the positive electrode plates is deemed as the ratio
N/P of the mass N of the negative electrode material to the mass P of the
positive electrode plate per lead-acid battery.
The content of barium contained in a formed negative active material
is quantitatively determined as follows. The lead-acid battery 2 in a
fully-charged condition is disassembled, and the negative electrode plate 4 is
washed with water, and then dried, to remove the sulfuric acid component.
Thus, the negative active material 14 is collected. The negative active
material is crushed, and hydrogen peroxide water having a concentration of
300 g/L is added thereto in an amount of 20 mL per 100 g of the negative
active material, and (1+3) nitric acid that is obtained by diluting 1 part by volume of 60 mass% concentrated nitric acid with 3 parts by volume of ion-exchange water is further added. The mixture is then heated with stirring for five hours to allow lead to dissolve in the form of lead nitrate.
Barium sulfate is further dissolved. The concentration of barium in the
resultant solution is quantitatively determined by atomic absorption
spectrometry, and the result is converted into the content of barium in the
negative active material. The content of barium in the negative active
material can then provide the content of barium sulfate in the negative
active material.
The contents of graphite and of carbon black contained in the formed
negative active material are quantitatively determined as follows. The
lead-acid battery 2 is in a fully-charged condition is disassembled, and the
negative electrode plate 4 is washed with water, and then dried, to remove
the sulfuric acid component. Thus, the negative active material 14 is
collected. The negative active material is crushed, and hydrogen peroxide
water having a concentration of 300 g/L is added thereto in an amount of 20
mL per 100 g of the negative active material, and (1+3) nitric acid that is
obtained by diluting 1 part by volume of 60 mass% concentrated nitric acid
with 3 parts by volume of ion-exchange water is further added. The
mixture is then heated with stirring for five hours to allow lead to dissolve in
the form of lead nitrate. Barium sulfate is further dissolved. Filtration is
then performed to separate graphite, carbon black, and the reinforcing
material.
Solid components obtained by filtration (graphite, carbon black, and
the reinforcing material) are dispersed in water. Using a sieve that retains
the reinforcing material, such as, for example, a sieve having an aperture of
1.4 mm, the dispersion solution is sieved twice, and then washed with water to remove the reinforcing material, thereby separating carbon black and graphite.
An organic shrink-proofing agent, such as lignin, is added to the
negative active material paste together with carbon black and graphite.
Due to the surface-active effect of the organic shrink-proofing agent, carbon
black and graphite remain in a non-aggregated state in the negative active
material even after formation. However, since the organic shrink-proofing
agent is dissolved in water and lost in the series of separation operations,
carbon black and graphite are dispersed in water, the organic
shrink-proofing agent is then added, and the mixture is stirred to
disaggregate again the aggregates of carbon black and of graphite, after
which the following separation operation is performed.
The organic shrink-proofing agent is not limited as long as it can be
added to a lead-acid battery. In Example, a lignin sulfonate Vanillex N
(manufactured by NIPPON PAPER INDUSTRIES CO., LTD.) was used. In
Example, 15 g of the organic shrink-proofing agent was added to 100 mL of
water, and a stirring operation was performed.
After the aforementioned operation, carbon black and graphite were
separated from each other by making suspension containing carbon black
and graphite pass through a sieve that does not substantially allow graphite
to pass therethrough, but allows carbon black to pass therethrough. In
Example, a sieve with an aperture of 20 pm was used. Even when graphite
having a particle size of less than this aperture is used, graphite having a
particle size of 3 pm or more causes clogging of the sieve, and thus such
graphite will not substantially pass through the sieve. After this operation, graphite remains on the sieve, and carbon black is contained in the liquid
that has passed through the sieve. Graphite and carbon black separated by the series of operations are washed with water and dried, and are then each weighed. Carbon fiber can be separated in a manner similar to that of graphite.
The average particle size (volume average size) of graphite is
measured by a light scattering method while the separated graphite is
dispersed again in water to which an organic shrink-proofing agent has been
added. A region corresponding to a particle size of less than 3 1m, if any, is
ignored as that of an impurity such as carbon black. Aluminum ions and
lithium ions in the electrolyte solution are quantitatively determined by
extracting the electrolyte solution, and then using ICP emission
spectrometry.
A permeation short circuit accelerating test and a PSOC life test
were conducted on the lead-acid battery 2 in a fully-charged condition.
Details of the PSOC life test are shown in Fig. 2 and in Table 1. The
denotation 1 CA means, for example, 30 A for a battery having a 5-hour rate
capacity of 30 Ah. The term 40 0 C air indicates that the test was conducted
in an air bath at 400 C. The number of cycles until the terminal voltage
reaches 1.2 V/cell in the test pattern in Table 1 is defined as a PSOC life.
Details of the permeation short circuit accelerating test are shown in Table 2.
This test is a test that is conducted under conditions that promote occurrence
of a permeation short circuit. Thus, the rate of occurrence of a permeation
short circuit is significantly higher than that under the actual conditions of
use of the lead-acid battery. Five cycles of the permeation short circuit
accelerating test pattern shown in Table 2 were conducted. After the 5
cycles, the lead-acid batteries were disassembled to determine the ratio of
lead-acid batteries in which short circuits have occurred. The term 250 C
water indicates that the test was conducted in a water bath at 25C. In
Tables 1 and 2, CC discharge, CV charge, and CC charge respectively mean
constant current discharge, constant voltage charge, and constant current
charge.
[Table 1] Test conditions Step Details Current and voltage Stop condition Temperature
1 CC discharge 1 CA 59 sec. 40°C air 2 CC discharge 300 A 1 sec. 40°C air 3 CV charge 2.4 V/cell, max. 50 A 10 sec. 40°C air 4 CC discharge 1 CA 5 sec. 40°C air 5 Repeat steps 3 and 4 5 times 40°C air 6 Repeat steps 1 - 5 50 times 40°C air 7 CV charge 2.4 V/cell, max. 50 A 900 sec. 40°C air 8 Repeat steps 1 - 7 72 times 40°C air 9 Rest 15h 40 0 Cair 10 Return to step 1 40 0 Cair
[Table 2] Test conditions Step Details Current and voltage Stop condition Temperature
1 CC discharge 0.05 CA 1.0 V/cell 25 0 C water
2 Left with Resistance 10 2 28 days 25 0 C water connected 3 CV charge 2.4 V/cell, max. 50 A 10 min. 25 0 C water 4 CC charge 0.05 CA 27 hours 25 0 C water 5 Repeat steps 1 - 4 5 times 25 0 C water
The results of the PSOC life test and of the permeation short circuit
accelerating test are shown in Tables 3 to 7, in which the percentages of the
contents are each a percentage by mass (mass%). Table 3 shows the results
when scalelike graphite was used, and Table 4 shows the results when
expanded graphite was used. In both cases, the negative active materials
did not contain carbon black, and the electrolyte solutions did not contain
aluminum ions nor lithium ions. The data of the PSOC life in Tables 3 and
4 are shown in relative values with respect to the values of the samples listed
on top of the respective tables, with these values defined as 100%.
[Table 3]
Mass of Mass of Scalelike graphite BaSO4 PSOC life Permeation Battery positive negative Average Number of short circuit no active active N/P ratio Content particle Content cycles (ratio occurrence material material (%) size (%) to Al defined rate (g/cell) (g/cell) (pm) as 100) (%) Al 338 320 0.95 100 40 A2 375 294 0.78 106 50 A3 420 261 0.62 0.5 150 0.6 110 60 A4 427 256 0.60 84 100 A5 331 325 0.98 80 40 A6 338 320 0.95 80 20 A7 375 294 0.78 84 20 A8 420 261 0.62 0 - 0.6 86 20 A9 427 256 0.60 78 20 A10 331 325 0.98 70 20 All 338 320 0.95 109 40 A12 375 294 0.78 2.0 150 0.6 114 60 A13 420 261 0.62 121 60 A14 338 320 0.95 110 100 3.0 150 0.6 A15 420 261 0.62 120 100 Bl 1.0 100 40 B2 1.2 104 0 B3 338 320 0.95 0.5 150 2.0 106 0 B4 3.0 106 0 B5 4.0 87 0 B6 1.2 107 0 B7 375 294 0.78 0.5 150 2.0 109 0 B8 3.0 109 0 B9 1.0 110 60 B10 1.2 113 0 Bll 420 261 0.62 0.5 150 2.0 114 0 B12 3.0 114 0 B13 4.0 90 0 B14 427 256 0.60 0.5 150 3.0 86 60 B15 331 325 0.98 0.5 150 3.0 84 0 B16 338 320 0.95 0 - 3.0 84 0 B17 420 261 0.62 0 - 3.0 89 0 B18 338 320 0.95 1.5 150 2.0 109 0 B19 1.0 109 40 B20 1.2 112 0 338 320 0.95 2.0 150 B21 3.0 115 0 B22 4.0 91 0 B23 1.2 120 0 375 294 0.78 2.0 150 B24 3.0 122 0 B25 420 261 0.62 1.5 150 2.0 121 0 B26 420 261 0.62 2.0 150 1.0 121 60
B27 1.2 125 10 B28 3.0 126 0 B29 4.0 96 0 B30 38 320 0.95 3.0 150 3.0 124 40 IB31 1 20 1 261 1 0.62 1 3.0 1 150 1 3.0 1 124 1 60
[Table 4] Mass of Mass of Expanded graphite BaSO4 POlie Permeation positive negative Average PS~ie short circuit Battery Number of cycles ocrec n. active active N/P ratio Content particle Content (ratio toDl occrrtenc material material N% size N% defined as 100) ____ (g/cell) (g/cell) _ ___ (Jim) ________ N____
Dl 338 320 0.95 100 30 D2 375 294 0.78 106 50 D3 420 261 0.62 0.5 150 0.6 108 50 D4 427 256 0.60 82 100 D5 331 325 0.98 _ __ ___ 78 40 D6 338 320 0.95 108 40 D7 375 294 0.78 2.0 150 0.6 116 50 D8 420 261 0.62 _ __ ___ 120 50 D9 338 320 0.95 30 10 .6109 100 D10 420 261 0.62 ____ ___ ___ 118 100 Dli 5 93 20 D2 338 320 0.95 0.5 10 0.6 103 D13 300 100 30 D14 ___________ 500 _ __ 91 50
D5 375 294 0.78 0.5 0.6 154 D16 ____________ 50 ___ 103 70 D17 5 110 40 D8 420 261 0.62 2.0 10 0.6 155 D19 300 116 60 D20 500 108 70 El 1.0 100 30 E2338 320 0.95 0.5 150 1.100 E3 3.0 lOS 0 E4 _______ 4.__0 84 0
E5375 294 0.78 0.5 150 1.100 E6 ____ _______ 3.0 110 0 E7 1.0 108 50 E8420 261 0.62 0.5 150 1.il0 E9 3.0 112 0 E10 1___ 4._______0 86 0 Eli 427 256 0.60 0.5 150 3.0 81 60 E12 331 325 0.98 0.5 150 3.0 80 0 E3 338 320 0.95 2.0 150 10154 E14 ____ ____ ____ ____ ___ 1.2 106 0
E15 3.0 102 0 E16 4.0 85 0 E17 1.2 115 0 375 294 0.78 2.0 150 E18 3.0 115 0 E19 1.0 117 50 E20 1.2 119 0 420 261 0.62 2.0 150 E21 3.0 120 0 E22 4.0 91 0 E23 338 320 0.95 3.0 150 3.0 118 40 E24 420 261 0.62 3.0 150 3.0 124 60 Fl 1.2 96 0 5 F2 3.0 95 0 F3 1.2 103 0 10 F4 3.0 105 0 338 320 0.95 0.5 F300 1.2 102 0 F6 3.0 102 0 F7 50 1.2 97 0 500 F8 3.0 95 0 F9 1.2 114 0 5 F10 3.0 115 0 F11 1.2 121 0 10 F12 3.0 120 0 420 261 0.62 2.0 F13300 1.2 119 10 F14 3.0 120 0 F500 1.2 111 10 F16 1 1 3.0 109 0
Fig. 3 and Table 3 show that inclusion of graphite in the negative
active material improves the PSOC life, and that inclusion of 0.5 mass% or
more of graphite significantly improves the PSOC life. On the other hand, it can be seen that inclusion of graphite in the negative active material
causes a permeation short circuit to easily occur. It was not known that
inclusion of graphite in the negative active material causes a permeation
short circuit to easily occur as described above.
Thus, the present inventors conducted studies on inhibition of
occurrence of a permeation short circuit while graphite is included in the
negative active material to improve the PSOC life. As a result, it has been
found that even when the negative active material contains graphite, an N/P ratio of 0.62 or more can inhibit a permeation short circuit (Fig. 4).
Meanwhile, when the negative active material does not contain graphite, the
effect of inhibiting a permeation short circuit cannot be obtained even when
the N/P ratio is 0.62 or more (Fig. 4). Thus, the effect of inhibiting a
permeation short circuit due to an N/P ratio of 0.62 or more is obtained only
when the negative active material contains graphite. It was not known that
graphite in the negative active material relates to a permeation short circuit,
nor that the N/P ratio relates to a permeation short circuit. Thus, it was not
foreseeable that using an N/P ratio of 0.62 or more when the negative active
material contains graphite could produce an effect of inhibiting a permeation
short circuit, and it is not easy for a person skilled in the art to get an idea of
using an N/P ratio of 0.62 or more to inhibit a permeation short circuit,
which occurs more easily by including graphite in the negative active
material.
Fig. 4 shows that when the negative active material contains
graphite, changing the N/P ratio from 0.6 to 0.62 markedly decreases the
permeation short circuit occurrence rate. It was obviously not foreseeable
that the N/P ratios of 0.6 and 0.62 have distinctly different effects of
inhibiting a permeation short circuit as described above, and it can be said
that an N/P ratio of 0.62 or more has a meaning as a critical point.
Fig. 5 shows that inclusion of graphite in the negative active material
improves the PSOC life, and that an N/P ratio in a range of 0.62 or more and
0.95 or less improves the PSOC life. More particularly, considering the fact
that inclusion of graphite in the negative active material and an N/P ratio in
a range of 0.62 or more and 0.95 or less together markedly improve the
PSOC life, it is found that the combination of inclusion of graphite in the
negative active material and an N/P ratio in a range of 0.62 or more and 0.95 or less can provide a synergetic effect (Fig. 5). An N/P ratio in a range of
0.62 or more and 0.78 or less further significantly improves the PSOC life.
Fig. 3 shows that a content of graphite in the negative active
material of 2.5 mass% or less can inhibit a permeation short circuit. Since
it was not known that graphite in the negative active material relates to
occurrence of a permeation short circuit, it is not easy for a person skilled in
the art to get an idea of using a content of graphite in the negative active
material of 2.5 mass% or less to inhibit a permeation short circuit. In
addition, Fig. 3 shows that a content of graphite in the negative active
material of 2.5 mass% or less markedly decreases the permeation short
circuit occurrence rate. Thus, it can be said that a content of graphite in the
negative active material of 2.5 mass% or less has a meaning as a critical
point. A content of graphite in the negative active material of 2.0 mass% or
less has a larger effect of inhibiting a permeation short circuit.
Table 3 and Fig. 6 show that inclusion of barium sulfate in the
negative active material produces an effect of inhibiting a permeation short
circuit. Since it was not known that barium sulfate in the negative active
material relates to a permeation short circuit, it was an unexpected result
that inclusion of barium sulfate in the negative active material produced an
effect of inhibiting a permeation short circuit. In particular, a content of
barium sulfate in the negative active material of 1.2 mass% or more
markedly improves the effect of inhibiting a permeation short circuit (Fig. 6).
Thus, it can be said that a content of barium sulfate in the negative active
material of 1.2 mass% or more has a meaning as a critical point.
Table 3 and Fig. 6 show that inclusion of barium sulfate in the
negative active material of more than 3.0 mass% markedly decreases the
PSOC life. Thus, the content of barium sulfate in the negative active material is preferably 3.0 mass% or less.
It can be seen that a content of graphite in the negative active
material of 2.5 mass% or less, a content of barium sulfate in the negative
active material of 1.2 mass% or more, and an N/P ratio of 0.62 or more can
yield a lead-acid battery having PSOC life performance higher than that of a
lead-acid battery not containing graphite in the negative active material,
and having excellent permeation short circuit resistance performance (e.g.,
samples B2 to B4 of Table 3). If any one of the content of graphite and the
content of barium sulfate in the negative active material and the N/P ratio is
outside the value range described above, a permeation short circuit cannot
be sufficiently inhibited.
For example, even when the content of barium sulfate in the negative
active material is 1.2 mass% or more, and the N/P ratio is 0.62 or more, a
permeation short circuit may not be sufficiently inhibited if the content of
graphite in the negative active material is more than 2.5 mass% (e.g.,
samples B30 and B31 of Table 3). In addition, even when the content of
graphite in the negative active material is 2.5 mass% or less, and the N/P
ratio is 0.62 or more, a permeation short circuit may not be sufficiently
inhibited if the content of barium sulfate in the negative active material is
less than 1.2 mass% (e.g., samples B1and B9 of Table 3). Similarlyeven
when the content of graphite in the negative active material is 2.5 mass% or
less, and the content of barium sulfate in the negative active material is 1.2
mass% or more, a permeation short circuit may not be sufficiently inhibited
if the N/P ratio is less than 0.62 (sample B14 of Table 3). Thus, concludingly, the combination of three configurations, that is, a content of graphite in the
negative active material of 2.5 mass% or less, a content of barium sulfate in
the negative active material of 1.2 mass% or more, and an N/P ratio of 0.62 or more, is required to sufficiently inhibit a permeation short circuit.
Since it was not known that graphite in the negative active material
relates to a permeation short circuit, it is not easy for a person skilled in the
art to get an idea of using a content of graphite in the negative active
material of 2.5 mass% or less to inhibit a permeation short circuit.
Moreover, since it was not known that barium sulfate in the negative active
material relates to a permeation short circuit, it is not easy for a person
skilled in the art to get an idea of using a content of barium sulfate in the
negative active material of 1.2 mass% or less to inhibit a permeation short
circuit. Furthermore, since it was also not known that the N/P ratio relates
to a permeation short circuit, it is not easy for a person skilled in the art to
get an idea of using an N/P ratio of 0.62 or more to inhibit a permeation short
circuit. Since it is not easy for a person skilled in the art to get each of the
ideas of using a content of graphite in the negative active material of 2.5
mass% or less, using a content of barium sulfate in the negative active
material of 1.2 mass% or less, and using an N/P ratio of 0.62 or more, it is
very difficult for a person skilled in the art to conceive of combining these
three configurations.
Table 4 shows that also when expanded graphite was used as
graphite, the results obtained were approximately the same as those
obtained when scalelike graphite was used as graphite.
Table 3 shows that even when the content of graphite in the negative
active material is 2.5 mass% or less, the content of barium sulfate in the
negative active material is 1.2 mass% or more, and the N/P ratio is 0.62 or
more, a permeation short circuit may not be completely inhibited (e.g.,
sample B27 of Table 3). Thus, the present inventors have conducted studies
on further inhibiting a permeation short circuit.
[Table 5] Mass of Mass of Scalelike graphite BaSO4 PSOC life Permeation Battery positive negative Average Number of short circuit n. active active N/P ratio Content particle Content cycles (ratio occurrence material material N% size %) to Aldefined rate (g/cell) (g/cell) _____ (Jim) as 100) N%
A16 5 96 30 Al7 10 101 40 Al 338 320 0.95 0.5 150 0.6 100 40 A18 300 100 40 A19 ________ ____ 500 95 50 A20 5 108 50 A2 375 294 0.78 0.5 150 0.6 106 50 A21 _______ ___ 500 107 70 A22 5 115 50 A23 10 119 60 A13 420 261 0.62 2.0 150 0.6 121 60 A24 300 120 60 A25 500 113 70 Cl 1.2 99 0 C2 _____ 3.0 98 0 Ca 1 1.2 104 0 C4 _____ 3.0 106 0
B2338 320 0.95 0.5 150 1.100 B4 _____ 3.0 106 0 CS 0 1.2 104 0 CC ____ 3.0 lOS 0 C7 50 1.2 100 0 C8 ___ ________ ___ 3.0 99 0 C9 5 1.2 110 0 ClO10__ 3.0 109 0 Cli 10 1.2 119 0 C12 _____ 3.0 121 0 B23 37 9 .8 20 10 1.2 120 0 B24 _____ 3.0 122 0 Ci330 1.2 120 0 C14 ___ 3.0 121 0 C1550 1.2 108 10 C16 ___ ________ ____ 30107 0 C17 5 1.2 119 0 C18 ___ 3.0 120 0 C19 10 1.2 123 0 C20 420 261 0.62 2.0 _____ 3.0 125 0 B27 10 1.2 125 10 B28 _____ 3.0 126 0 C21 ________ ___ ____ 300 1.2 123 10
C22 3.0 124 0 C23 1.2 118 10 C24 3.0 118 0
Table 5 and Fig. 7 show effects of the average particle size of graphite
in the negative active material. It can be seen that an average particle size
of graphite in the negative active material of 300 pm or less can inhibit a
permeation short circuit. It was an unexpected result that use of an
average particle size of graphite in the negative active material of 300 pm or
less can inhibit a permeation short circuit. More particularly, a content of
graphite in the negative active material of 2.5 mass% or less, a content of
barium sulfate in the negative active material of 1.2 mass% or more, an N/P
ratio of 0.62 or more, and an average particle size of graphite in the negative
active material of 300 pm or less can together yield a lead-acid battery in
which occurrence of a permeation short circuit is almost completely inhibited.
It was not known that the average particle size of graphite in the negative
active material relates to a permeation short circuit. Thus, even if a person
skilled in the art attempts to obtain a lead-acid battery having excellent
permeation short circuit resistance performance, a large number of
trial-and-error steps are required to get the ideas of using a content of
graphite in the negative active material of 2.5 mass% or less, using a content
of barium sulfate in the negative active material of 1.2 mass% or more, using
an N/P ratio of 0.62 or more, and using an average particle size of graphite in
the negative active material of 300 pm or less. Such a combination of ideas
cannot occur easily.
Table 5 and Fig. 7 show that an average particle size of graphite in
the negative active material of 10 pm or more markedly improves the PSOC
life.
[Table 6] Graphite BaSO4 CrbonPSOC life Permeation pos negatfblack Number of short Battery positive negative N/P Average cycles (ratio circuit no. ate ate ratio Content particle Content Content to Al occurrence (%) size (%) (%) defined as rate (g/cell) (g/cell) (pm) 100) (%)
B27 0 125 10
Gi 0.05 127 0
G2 0.1 128 0 420 261 0.62 Scalelike 2.0 150 1.2 G3 0.3 134 0
G4 0.5 137 0
G5 1.0 137 0
G6 0 120 10
G7 375 294 0.78 Scalelike 1.5 300 1.2 0.05 123 0
G8 0.5 131 0
Table 6 and Fig. 8 show effects of carbon black in the negative active
material. It can be seen that inclusion of carbon black in the negative active
material can inhibit a permeation short circuit. It was an unexpected result
that inclusion of carbon black in the negative active material can inhibit a
permeation short circuit. More particularly, it can be seen that a content of
graphite in the negative active material of 2.5 mass% or less, a content of
barium sulfate in the negative active material of 1.2 mass% or more, an N/P
ratio of 0.62 or more, and inclusion of carbon black in the negative active
material can together yield a lead-acid battery in which occurrence of a
permeation short circuit is almost completely inhibited. It was not known
that carbon black in the negative active material relates to a permeation
short circuit. Thus, even if a person skilled in the art attempts to obtain a
lead-acid battery having excellent permeation short circuit resistance
performance, a large number of trial-and-error steps are required to get the
ideas of using a content of graphite in the negative active material of 2.5 mass% or less, using a content of barium sulfate in the negative active material of 1.2 mass% or more, using an N/P ratio of 0.62 or more, and including carbon black in the negative active material. Such a combination of ideas cannot occur easily.
The effect of carbon black of inhibiting a permeation short circuit is
noticeable when the content of carbon black in the negative active material is
0.05 mass% or more (Fig. 8). Meanwhile, inclusion of carbon black in the
negative active material of more than 1.0 mass% made the active material
paste too hard to fill therewith the negative electrode current collector.
A content of carbon black in the negative active material of 0.1
mass% or more produces a larger effect of improving the PSOC life than
when the content of carbon black in the negative active material is less than
0.1 mass% (Fig. 8). A content of carbon black in the negative electrode
material of 0.5 mass% or more produces an especially large effect of
improving the PSOC life. Note that the electrolyte solutions of Table 6 did
not contain aluminum ions nor lithium ions. Scalelike graphite was used as
graphite in Table 6, but similar results were obtained when expanded
graphite was used.
C-~ ~ C ~ S C C).~ C)~ ) C)QN NC) C - C - C - C - ; C C C C C C N a C) Q~ 4 ______
C) - C - C ~ Qc
in ~ ci at in in r- r- ~ C C
cit~ ~ S Nj~ C)
ci 2 a5 at 6 C C C 6 0
6 C C
C I~______ -
C ~
C C C C
6 6
tfl ~NR ci c~ C U
C)
bE
C) ;~. .~ -~- 8 C)
~-1
C) C C ~ Cz~ ci C) C N Q
C) C) C)
cit
C ci ~C) N 6 C)
C- ~
~C) ~C) CO C)bL ci bE C) C C)
o (flC)C)C) C C) ci ~:~~ !
C C) - C)
ci - ci ~c in cc ~ C
Table 7 shows effects of aluminum ions and effects of lithium ions in
the electrolyte solution. In Table 7, the negative active material did not
contain carbon black. Scalelike graphite was used as graphite in Table 7, but similar results were obtained when expanded graphite was used.
Inclusion of aluminum ions in the electrolyte solution improves the PSOC
life (samples H1 to H4 of Table 7, and Fig. 9). Inclusion of 0.02 mol/L or
more of aluminum ions in the electrolyte solution significantly improves the
PSOC life (samples H1 to H4 of Table 7, and Fig. 9). Inclusion of 0.2 mol/L
or less of aluminum ions in the electrolyte solution also significantly
improves the PSOC life (samples H1 to H4 of Table 7, and Fig. 9).
Table 7 and Fig. 10 show that inclusion of lithium ions in the
electrolyte solution can inhibit a permeation short circuit. More
particularly, a content of graphite in the negative active material of 2.5
mass% or less, a content of barium sulfate in the negative active material of
1.2 mass% or more, an N/P ratio of 0.62 or more, and inclusion of lithium
ions in the electrolyte solution together yielded a lead-acid battery in which
occurrence of a permeation short circuit was almost completely inhibited.
Even if a person skilled in the art attempts to obtain a lead-acid battery
having excellent permeation short circuit resistance performance, a large
number of trial-and-error steps are required to get the ideas of using a
content of barium sulfate in the negative active material of 1.2 mass% or
more, using an N/P ratio of 0.62 or more, and including lithium ions in the
electrolyte solution. Such a combination of ideas cannot occur easily. The
effect of inhibiting a permeation short circuit by lithium ions is noticeable
when the concentration of lithium ions in the electrolyte solution is 0.02
mol/L or more.
Inclusion of 0.1 mol/L or more of lithium ions in the electrolyte solution improves the PSOC life (samples H5 to H8 of Table 7, and Fig. 10).
In addition, inclusion of 0.2 mol/L or less of lithium ions in the electrolyte
solution improves the PSOC life (samples H5 to H8 of Table 7, and Fig. 10).
Inclusion of both aluminum ions and lithium ions in the electrolyte
solution can inhibit a permeation short circuit, and significantly improves
the PSOC life (samples H9 and H10 of Table 7).
In Example, a lead-acid battery which is excellent in PSOC life and
suffers little permeation short circuit is obtained, and a glass mat etc. may
be used as a separator to produce a valve-regulated lead-acid battery.
Throughout this specification and the claims which follow, unless the
context requires otherwise, the word "comprise", and variations such as "comprises" and "comprising", will be understood to imply the inclusion of a
stated integer or step or group of integers or steps but not the exclusion of
any other integer or step or group of integers or steps.
The reference to any prior art in this specification is not, and should
not be taken as, an acknowledgement or any form of suggestion that the
prior art forms part of the common general knowledge in Australia.

Claims (12)

What is claimed is:
1. A lead-acid battery comprising:
a negative electrode plate;
a positive electrode plate; and
an electrolyte solution,
wherein the negative electrode plate includes a negative electrode
material containing graphite or carbon fiber,
a ratio N/P of a mass N of the negative electrode material to a mass P
of a positive electrode material per lead-acid battery is 0.62 or more,
the negative electrode material contains 1.75 mass% or less of
elemental barium in a fully-charged condition,
the ratio N/P is 0.95 or less, and
the negative electrode material contains 2.5 mass% or less of
graphite or 2.5 mass% or less of carbon fiber.
2. The lead-acid battery according to claim 1, wherein the negative
electrode material contains barium sulfate.
3. The lead-acid battery according to claim 1, wherein the negative
electrode material contains elemental barium.
4. The lead-acid battery according to claim 2, wherein the negative
electrode material contains 1.2 mass% or more of barium sulfate.
5. The lead-acid battery according to claim 1, wherein the negative
electrode material contains 0.7 mass% or more of elemental barium.
6. The lead-acid battery according to any one of claims 2 to 5, wherein
the negative electrode material contains 3.0 mass% or less of barium sulfate.
7. The lead-acid battery according to any one of claims 1 to 6, wherein
the negative electrode material contains carbon black.
8. The lead-acid battery according to any one of claims 1 to 7, wherein
the graphite or the carbon fiber is graphite having an average particle size of
300 pm or less.
9. The lead-acid battery according to any one of claims 1 to 8, wherein
the graphite or the carbon fiber is graphite having an average particle size of
10 pm or more.
10. The lead-acid battery according to any one of claims 1 to 9, wherein
the electrolyte solution contains aluminum ions.
11. The lead-acid battery according to any one of claims 1 to 10, wherein
the electrolyte solution contains lithium ions.
12. The lead-acid battery according to any one of claims 1 to 11, wherein
the ratio N/P is 0.78 or less.
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Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2018100635A1 (en) * 2016-11-29 2018-06-07 日立化成株式会社 Lead storage battery and production method therefor
WO2018199242A1 (en) * 2017-04-28 2018-11-01 株式会社Gsユアサ Lead acid storage battery
WO2018199207A1 (en) * 2017-04-28 2018-11-01 株式会社Gsユアサ Lead acid battery
JP7099448B2 (en) * 2017-04-28 2022-07-12 株式会社Gsユアサ Lead-acid battery
EP3633781B1 (en) * 2017-07-24 2024-04-24 GS Yuasa International Ltd. Lead-acid battery
WO2019188056A1 (en) 2018-03-29 2019-10-03 株式会社Gsユアサ Lead acid storage battery
EP3975289A4 (en) 2019-05-31 2022-11-16 GS Yuasa International Ltd. Lead acid storage battery
JPWO2024005041A1 (en) 2022-06-30 2024-01-04
JP2024044869A (en) * 2022-09-21 2024-04-02 エナジーウィズ株式会社 Lead-acid battery

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0352115A1 (en) * 1988-07-21 1990-01-24 Yuasa Corporation Lead-acid battery
JP2006049025A (en) * 2004-08-03 2006-02-16 Furukawa Battery Co Ltd:The Control valve type lead-acid storage battery
JP5190562B1 (en) * 2011-09-30 2013-04-24 パナソニック株式会社 Lead-acid battery for energy storage
JP2015005528A (en) * 2014-09-05 2015-01-08 株式会社Gsユアサ Lead storage battery

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0244658A (en) * 1988-08-04 1990-02-14 Yuasa Battery Co Ltd Sealed lead-acid battery
JP3094423B2 (en) * 1990-05-31 2000-10-03 松下電器産業株式会社 Lead storage battery
JP5396216B2 (en) * 2009-09-25 2014-01-22 古河電池株式会社 Lead acid battery
TW201136010A (en) * 2010-01-21 2011-10-16 Gs Yuasa Int Ltd Negative electrode plate using in lead storage cell, fabricating method thereof, and lead storage cell
WO2012042917A1 (en) * 2010-09-30 2012-04-05 新神戸電機株式会社 Lead storage battery
JP5708959B2 (en) * 2014-09-08 2015-04-30 株式会社Gsユアサ Lead acid battery

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0352115A1 (en) * 1988-07-21 1990-01-24 Yuasa Corporation Lead-acid battery
JP2006049025A (en) * 2004-08-03 2006-02-16 Furukawa Battery Co Ltd:The Control valve type lead-acid storage battery
JP5190562B1 (en) * 2011-09-30 2013-04-24 パナソニック株式会社 Lead-acid battery for energy storage
JP2015005528A (en) * 2014-09-05 2015-01-08 株式会社Gsユアサ Lead storage battery

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