Patent Application
20160240857
This application claims the benefit of Japanese patent applications No. 2015-029555, filed on Feb. 18, 2015, and No. 2015-248243, filed on Dec. 21, 2015, which are incorporated by reference,
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.
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.
The following presents a simplified summary of the invention disclosed herein in order to provide a basic understanding of some aspects of the invention. This summary is not an extensive overview of the invention. It is intended to neither identify key or critical elements of the invention nor delineate the scope of the invention. Its sole purpose is to present some concepts of the invention in a simplified form as a prelude to the more detailed description that is presented later,
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:
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 foregoing and other features of the present invention will become apparent from the following description and drawings of an illustrative embodiment of the invention in which:
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 μm or more and 500 μm 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 MP ratio is 0.62 or more, a permeation short circuit :nay 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 μm 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 μm or less.
An average particle size of graphite in the negative electrode material of 10 μm or more improves the PSOC life, and thus the average particle size of graphite in the negative electrode material is preferably 10 μm 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).
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 μm or more and 300 μm 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 Ω·cm to 0.01 Ω·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 μm, and an average secondary particle size of 2.5 μm. 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 μm or more and 2.0 μm or less, and an average secondary particle size of, for example, 1.0 μm or more and 10 μm 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)×100 mm (width)×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/cm3 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)×100 mm (width)×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/cm3 or more and 4.8 g/cm3 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, 0.5 mm or more and 0.9 mm 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.
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 μm was used. Even when graphite having a particle size of less than this aperture is used, graphite having a particle size of 3 μm 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 μm, 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
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%.
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 (
Table 3 and
Table 3 and
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 B1 and B9 of Table 3). Similarly, even 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 and
Table 5 and
Table 6 and
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 (
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 % (
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
Table 7 and
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
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.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2015-029555 | Feb 2015 | JP | national |
| 2015-248243 | Dec 2015 | JP | national |
