Patent Application
20120258336
The present invention relates to a hybrid negative plate for a lead-acid storage battery suitable for hybrid automobile applications repeating rapid charge and discharge in PSOC and industrial applications such as windmills and PV (photovoltaics), and a lead-acid storage battery.
JP-T-2007-506230 (the term “JP-T” as used herein means a published Japanese translation of a PCT patent application) proposes an invention that by using a hybrid negative plate comprising a negative plate comprising a porous collecting plate and a lead active material filled therein, and having formed on the surface thereof, a coating layer of a carbon mixture comprising two kinds of carbon materials comprising a first carbon material such as conductive carbon black, and a second carbon material such as activated carbon or graphite, having capacitor capacity and/or pseudocapacitor capacity, and a binder, as a negative electrode of a lead-acid storage battery, in the case of repeating rapid charge and discharge in PSOC of a lead-acid storage battery, life can greatly be prolonged by the function of the capacitor as compared with a lead-acid storage battery equipped with the conventional negative plate.
However, it became clear in the lead-acid storage battery that because an amount of hydrogen gas evolved from a negative electrode during charging is determined by hydrogen overvoltage of the negative electrode, formation of a coating layer of the above-described carbon mixture having a large surface area and low hydrogen overvoltage on the surface of a negative electrode active material-filled plate as described in Patent Document 1 above promotes hydrogen gas evolution, leading to decrease in an electrolyte due to water electrolysis during charging. To inhibit this phenomenon, Patent Document 1 discloses increasing hydrogen overvoltage by mixing additives such as lead, zinc, bismuth, silver and their compounds to the carbon mixture. Hydrogen overvoltage of a negative electrode can be increased by the addition of those additives, but the increased hydrogen voltage is not yet sufficient. As a result of investigations, it was found that particularly when activated carbon is used as a second carbon material, hydrogen overvoltage cannot be increased, and properties of the activated carbon itself greatly affect the presence or absence of appearance of the effect of increasing hydrogen overvoltage.
The present invention has been made based on the finding. The present invention has an object to overcome the problems in the above-described conventional invention, and to provide a hybrid negative plate for a lead-acid storage battery, that inhibits decrease in hydrogen overvoltage and additionally inhibit water reduction by increasing hydrogen overvoltage, based on the improvement of activated carbon, leading to improvement in cycle characteristics of a lead-acid storage battery, and a lead-acid storage battery using the hybrid negative plate.
The present invention provides a hybrid negative plate for a lead-acid storage battery, comprising a negative electrode active material-filled plate having formed on the surface thereof a coating layer of a carbon mixture comprising a carbon material for ensuring conductivity, activated carbon for ensuring capacitor capacity and/or pseudocapacitor capacity, and at least a binder, wherein the activated carbon is activated carbon modified with a functional group, as described in claim 1.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 1, wherein the activated carbon modified with a functional group contains a volatile component in an amount of 3 to 30% by weight, as described in claim 2.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 1, wherein the carbon mixture comprises 5 to 70 parts by weight of the carbon material, 20 to 80 parts by weight of the activated carbon, 1 to 20 parts by weight of the binder, 0 to 10 parts by weight of a thickener, and 0 to 10 parts by weight of a short fiber-like reinforcement, as described in claim 3.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 1, wherein an amount of the carbon mixture applied to the surface of the negative electrode active material-filled plate is 15 parts by weight or less relative to 100 parts by weight of the negative electrode active material, as described in claim 4.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 1, wherein the carbon mixture coating layer has a porosity of 40 to 90%, as described in claim 5.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 1, wherein the carbon mixture coating layer has a thickness of 0.1 mm or less, as described in claim 6.
The present invention provides a lead-acid storage battery comprising the hybrid negative plate described in any one of claims 1 to 6, as described in claim 7.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in any one of claims 1 to 3, wherein the activated carbon modified with a functional group is an acidic surface functional group, as described in claim 8.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 8, wherein an amount of the acidic surface functional group is that a value obtained by dividing the amount thereof per 1 g of the activated carbon by a specific surface area of the activated carbon is 0.16 to 3.11 μmol/m2, as described in claim 9.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 9, wherein the acidic surface functional group is a carboxyl group, and an amount of the carboxyl group per 1 g of the activated carbon is that a value divided by a specific surface area of the activated carbon is 0.01 μmol/m2 or more, as described in claim 10.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 9, wherein the acidic surface functional group is a lactone group, and an amount of the lactone group per 1 g of the activated carbon is that a value divided by a specific surface area of the activated carbon is 0.04 μmol/m2 or more, as described in claim 11.
The present invention provides the hybrid negative plate for a lead-acid storage battery described in claim 9, wherein the acidic surface functional group is a phenolic hydroxyl group, and an amount of the phenolic hydroxyl group per 1 g of the activated carbon is that a value divided by a specific surface area of the activated carbon is 0.14 μmol/m2 or more, as described in claim 12.
The present invention provides a lead-acid storage battery comprising the hybrid negative plate described in any one of claims 8 to 12, as described in claim 13.
According to the invention described in claim 1, the lead-acid storage battery comprising the hybrid negative plate can inhibit decrease in hydrogen overvoltage, leading to, for example, improvement of rapid charge and discharge cycle characteristics in PSOC. Thus, the lead-acid storage battery is suitable for use in hybrid automobiles repeating on/off action of an engine and industries utilizing various batteries, such as windmills, and brings about excellent effect.
The invention according to claim 2 can increase hydrogen overvoltage of the negative electrode, and additionally, can decrease internal resistance. The invention further inhibits precipitation of lead. Thus, the invention provides a lead-acid storage battery having excellent battery characteristics.
The invention according to claim 3 can secure good conductivity and capacitor capacity of the negative electrode by that the amount of the first carbon material is 5 to 70 parts by weight.
The invention can secure capacitor capacity by that the amount of the activated carbon modified with a functional group is 20 to 80 parts by weight.
The invention can secure electrical connection between the carbon mixture coating layer and the surface of the negative electrode active material-filled plate, and conductivity, and further can maintain the carbon mixture coating layer in a good porous state by that the amount of binder is 1 to 20 parts by weight.
In the invention according to claim 3, the amounts of the thickener and the short fiber-like reinforcement are 10 parts by weight or less, respectively, and the amount is effective to prepare the carbon mixture in a paste state without deterioration of conductivity. Furthermore, the short fiber-like reinforcement can prevent cracks of the carbon mixture coating layer during drying.
The invention according to claim 4 can surely form the carbon mixture coating layer having an appropriate thickness, leading to the above effect.
The invention according to claim 5 can secure movement of an electrolyte and therefore can secure good discharge performance, by that the carbon mixture coating layer has a porosity of 60 to 90%.
The invention according to claim 6 brings about economically sufficient discharge effect by that the carbon mixture coating layer has a thickness of 1.0 mm or less.
According to the invention described in claim 7, the lead-acid storage battery can be used in hybrid automobiles repeating on-of operations of an engine, and various industries utilizing a battery, such as windmills, thereby rapid charge and discharge cycle characteristics can be improved.
The inventions according to claims 8 to 12 increase electrostatic capacity of the hybrid negative plate. The lead-acid storage battery comprising each of those hybrid negative plates, described in claim 13 improves charge acceptability, and this leads to improvement of cycle characteristics. Furthermore, hydrogen overvoltage of the hybrid negative plate is increased, and water reduction is inhibited, leading to improvement of cycle characteristics.
The embodiment of the present invention is described in detail below.
When activated carbon selected as a second carbon material to be mixed with the first carbon material is generally used as activated carbon for an electric double layer capacitor, the activated carbon is subjected to a treatment for removing a surface functional group thereof by, for example, high temperature treatment in order to improve durability of the activated carbon. The reason for this is that when an organic electrolyte is used, a surface functional group of activated carbon brings in moisture to a system, and the moisture remarkably deteriorates durability. It is further said that in an aqueous capacitor, the moisture causes a metal material used in a substrate to corrode and elute, and the resulting impurity ions deteriorate durability.
However, the present inventors have found that a surface functional group of activated carbon, that has conventionally been considered unnecessary to be present, plays a critical role in increasing hydrogen overvoltage.
More specifically, a carbon mixture comprising carbon black for ensuring conductivity as a first carbon material, the conventional activated carbon, PP as a binder, and water as a dispersant was applied to the surface of a negative plate of a lead-acid storage battery, that is, a lead active material-filled plate, followed by drying. Thus, a hybrid negative electrode having formed thereon a porous carbon mixture coating layer was prepared. The hybrid negative electrode thus prepared was used as a negative electrode of a lead-acid storage battery, and charge and discharge were repeated. In the course of charge-discharge repetition, it was expected that lead ions dissolved from the hybrid negative electrode gradually precipitate on the surface of the porous carbon mixture coating layer to form layers of metallic lead and/or lead sulfate, and as a result, hydrogen overvoltage of the negative electrode is increased to a level of a negative electrode free of a carbon mixture coating layer.
However, the fact was that when the amount of a surface functional group of activated carbon is small, lead ions do not sufficiently precipitate, and even though charge and discharge are repeated, hydrogen overvoltage is not increased. In view of this fact, by way of experiment, each of activated carbons in which the amount of a surface functional group had gradually been increased was contained in a carbon mixture, many negative electrodes were prepared in the same manner as above, lead-acid storage batteries having the respective negative electrodes therein were produced, and the state of the negative electrodes after repeating charge and discharge was examined, respectively. As a result, it was confirmed that metallic lead and/or lead sulfate layers are sufficiently formed on the surface of the carbon mixture coating layer, and hydrogen overvoltage of the respective negative electrodes is increased.
As a result of further experimentations and researches from the above standpoint, the conclusion was obtained that the amount of a surface functional group of activated carbon brings about the effect of increasing hydrogen overvoltage in an amount of a specific range described below. Consequently, the conventional activated carbon is considered as activated carbon that is not modified with a surface functional group, and activated carbon characterized in the present invention, as described in claim 1 is expressed as “activated carbon modified with a functional group” and is distinguished from the conventional activated carbon.
Conventionally, it is considered that the amount of a surface functional group can be quantitatively determined by XSP (X-ray photoelectron spectroscopy) and a titration method for a specific functional group, but the quantitative determination requires high technique and is generally difficult to perform. As a result of intensive investigations in view of the circumstance, the present inventors have given thought to use a quantitative value of a volatile component defined in JIS M 8812 as an alternative characteristic. Porous carbon mixture coating layers containing various activated carbons having different amount of a functional group were formed on negative electrodes, respectively, and hydrogen overvoltage of the respective negative electrodes was measured by cyclic voltammogram. As a result, when activated carbon contains a volatile component in an amount of 3% by weight or more, hydrogen overvoltage is increased, but when the amount of the volatile component is increased and exceeds 30% by weight, capacitor capacity is decreased. It has been clarified from this fact that the amount of the volatile component is preferably in a range of from 3 to 30% by weight, and more preferably from 4 to 25% by weight, and durability is not deteriorated.
The preferred carbon mixture of the present invention has a composition comprising 5 to 70 parts by weight of the first carbon material, 20 to 80 parts by weight of the activated carbon, 1 to 10 parts by weight of the binder, 1 to 10 parts by weight of the thickener, and 0 to 10 parts by weight of the short fiber-like reinforcement.
The first carbon material is necessary to ensure conductivity, and suitable examples of the first carbon material include carbon black such as acetylene black and furnace black, Ketjen black and graphite. From the standpoint of emphasis on conductivity, the carbon material preferably contains a small amount of the surface functional group. Where the amount of the first carbon material added is less than 5 parts by weight, conductivity cannot be ensured, leading to decrease in capacitor capacity. On the other hand, the amount exceeds 70 parts by weight, conductive effect is saturated. The amount of the first carbon material is more preferably 10 to 60 parts by weight.
The activated carbon is necessary to ensure capacity as capacitor and/or pseudocapacitor. From the standpoint of ensuring capacitor and/or pseudocapacitor capacities, where the amount of the activated carbon added is less than 20 parts by weight, capacitor capacity is insufficient, and on the other hand, where the amount thereof exceeds 80 parts by weight, the proportion of the first carbon material is relatively decreased, and capacity is rather decreased. The amount of the activated carbon is more preferably 30 to 70 parts by weight.
The binder is necessary to bond carbon materials to each other and bond the carbon materials to a surface of the negative electrode constituting a lead-acid storage battery to thereby ensure electrical connection, and additionally, to maintain the mixture in a porous state. Suitable examples of the binder include polychloroprene, SBR, PTFE and PVDF. Where the amount of the binder is less than 1 part by weight, the bonding is insufficient, and on the other hand, where the amount thereof exceeds 20 parts by weight, the bonding effect becomes saturated, and further because the binder is an insulating material, the binder decreases conductivity. The amount of the binder is more preferably 5 to 15 parts by weight.
The thickener is useful to prepare a paste-like mixture. Suitable examples of an aqueous paste include cellulose derivatives such as CMC and MC, polyacrylate and polyvinyl alcohol, and suitable examples of an organic paste include NMP (N-methyl-2-pyrrolidone) and 1-methyl-2-pyrrolidone. In the case of using the thickener, when dry residue exceeds 10 parts by weight, conductivity of the mixture is deteriorated. Therefore, the amount of the thickener should not exceed 10 parts by weight.
The short fiber-like reinforcement is effective to inhibit occurrence of cracks due to drying when the mixture is prepared into a paste and the paste is applied to a negative electrode. A material of the reinforcement is required to be stable in sulfuric acid acidity, and examples thereof include carbon, glass, PET (polyethylene terephthalate) and polyester. The reinforcement desirably has a size of 20 μm or less and a length of 0.1 mm to 4 mm. Where the amount of the reinforcement added exceeds 10 parts by weight, the amount decreases relative ratios of the carbon material and the binder, resulting in deterioration of performance, and further decreases conductivity. Therefore, the amount of the reinforcement should not exceed 10 parts by weight.
The amount of the carbon mixture added is preferably 15 parts by weight or less relative to 100 parts by weight of the negative electrode active material. Where the amount of the carbon mixture exceeds 15 parts by weight, thickness of the coating layer is increased and the effect becomes saturated. The amount of the carbon mixture is more preferably 3 to 10 parts by weight.
The porous carbon mixture coating layer covering the negative electrode active material-filled plate has a porosity of preferably 40 to 90%. Where the porosity is less than 40%, movement of an electrolyte is inhibited, leading to decrease in discharge performance. On the other hand, where the porosity exceeds 90%, the effect becomes saturated, and additionally, a thickness of the coating layer is increased, resulting in designing trouble. The porosity is more preferably 60 to 80%.
The carbon mixture coating layer has a thickness of 1.0 mm or less. Even where the thickness exceeds 1.0 mm, the discharge characteristic effect becomes saturated, and further improvement is not achieved. For this reason, the thickness of 1.0 mm or less brings about the above effect with economy.
Respective hydrogen gas evolution potentials of six kinds of activated carbons each containing a volatile component in a different amount of 2.5%, 3.0%, 3.2%, 4.1%, 4.8% and 5.3% by weight were examined in the following manner.
The six kinds the activated carbons were used as compounding ingredients of the carbon mixture shown in Table 1 below, and six kinds of the carbon mixtures were prepared as Sample Nos. 1 to 6. Each of the six kinds of the carbon mixture samples was applied to both surfaces of a 2 cm square pure lead plate in the total amount of 0.5 g. The plate was sandwiched between AGM (Absorbed Glass Mat) separators, and counter electrodes comprising lead dioxide were stacked on the both sides to prepare a stack (laminate). The stack was sandwiched between acrylic plates, and fixed such that a pressure of 20 kPa is applied thereto. The stack was placed in a sulfuric acid aqueous solution having specific gravity of 1.30 and a temperature of 25° C., charge and discharge by cyclic voltammogram were repeated 10 times at a scan rate of 10 mV/sec in a range of −1.6V to +1.0V vs. Hg/Hg2SO4, and cathode potential due to hydrogen evolution initiation at 10th cycle was measured. The results are shown in Table 2 below.
On the other hand, for the sake of comparison, a 2 cm square pure lead plate to which a carbon mixture is not applied was used as a comparative sample. The comparative sample was sandwiched between an AGM separator and lead dioxide to prepare a stack, and the resulting stack was sandwiched between acrylic plates, and fixed such that a pressure of 20 kPa is applied thereto. Charge and discharge were repeated 10 times under the same conditions as above, and cathode potential due to hydrogen evolution at 10th cycle was measured. The results are shown in Table 2. It was clarified from Table 2 that hydrogen gas evolution potential is increased with increasing the amount of the volatile component in activated carbon, and when the amount of the volatile component is 3.0% by weight or more, problem-free hydrogen gas evolution potential as a lead-acid storage battery is obtained.
In Table 1, Table 2, and Table 3 described hereinafter, the activated carbon modified with a functional group was simply indicated as activated carbon.
The conventional formed positive plate and formed negative plate used in a valve-regulated lead-acid storage battery were prepared by the conventional method. Each of six kinds of carbon mixtures comprising the common formulation composition shown in Table 1 and each of six kinds of activated carbons each containing a volatile component in a different amount of 2.5%, 3.0%, 3.2%, 4.1%, 4.8% and 5.3% by weight was applied to both surfaces of each of the formed negative plates thus produced, followed by drying at 60° C. for 1 hour in the air. Thus, six kinds of hybrid negative plates having a porous carbon mixture coating layer having a porosity of 75% were produced.
Each of the six kinds of the hybrid negative plates produced above was used as a negative electrode. The negative plate was laminated with the positive electrode and AMG separator to assemble a plate group, and the plate group was put in a battery case of a valve-regulated lead-acid storage battery in the same manner as in the conventional assembling method. Thus, six kinds of lead-acid storage batteries having 5-hour rate capacity of 10 Ah in capacity control of positive electrode were assembled. Degree of compression of the plate group was adjusted by inserting a spacer between the battery case and the plate group as to be 50 kPa.
For the sake of comparison, a negative electrode active material-filled plate comprising a filling porous collecting substrate to which a carbon mixture is not applied, and a lead active material filled therein was used as a negative electrode, and a plate group was prepared in the same manner as above. The plate group was put in a battery case such that the degree of compression is 50 kPa. Thus, the conventional 2V lead-acid storage battery having 5-hour rate capacity of 10 Ah was assembled.
A sulfuric acid aqueous solution having specific gravity of 1.30 prepared by dissolving 30 g/liter of aluminum sulfate octadeca hydrate in water was poured as an electrolyte in each of the six kinds of the lead-acid storage battery Nos. 1 to 6 assembled above and the above lead-acid storage battery for comparison. Those batteries were charged at 1 A for 20 hours, and then discharged at 2 A until battery voltage reaches 1.75V. The batteries were again charged at 1 A for 15 hours and then discharged at 2 A until a cell voltage of 1.75V, and 5-hour rate capacity of the batteries was measured. As a result, the capacity of all of those batteries was 10 Ah.
Each of the six kinds of the lead-acid storage battery Nos. 1 to 6 above and the conventional lead-acid storage battery above were subjected to a life test by repeating rapid charge and discharge in PSOC in the form of the simulation of running by HEV. Specifically, the testis as follows. Each lead-acid storage battery was discharged at 2 A for 1 hour to make 80% of PSOC. Discharging at 50 A for 1 second and charging at 20 A for 1 second were repeated 500 times in the atmosphere of 40° C., and charging at 30 A for 1 second and pausing for 1 second were repeated 510 times. Those operations were taken as one cycle. This test was repeated 400 cycles, and internal resistance of the lead-acid storage battery was measured. The results are shown in Table 3. The conventional lead-acid storage battery came to the end of its life in 180 cycles, and the internal resistance thereof could not be measured. As is apparent from Table 3, it has been seen that the internal resistance is decreased and the battery performance is improved, with increasing the amount of a volatile component of the activated carbon.
Each of carbon mixtures having the formation composition shown in Table 1 was prepared using each of seven kinds of activated carbons containing a volatile component in a different amount of from 3.0% by weight to 36.2% by weight as shown in Table 4 below. Each of the seven kinds of the carbon mixtures was applied to both surfaces of a 2 cm square pure lead plate in the total amount of 0.5 g in the same manner as in Example 2. The plate was sandwiched between AGM separators, and counter electrodes comprising lead dioxide were provided on the both sides to prepare a stack. The stack was sandwiched between acrylic plates, and fixed such that a pressure of 20 kPa is applied thereto. Each of seven kinds of stack (negative electrode) sample Nos. 7 to 13 was placed in a sulfuric acid aqueous solution having specific gravity of 1.30 and a temperature of 25° C., charge and discharge by cyclic voltammogram were repeated 10 times at a scan rate of 10 mV/sec in a range of −1.6V to +1.0V vs. Hg/Hg2SO4, and cathode potential due to hydrogen evolution initiation at 10th cycle was measured. Furthermore, coulomb amount at the 10th cycle in a range (−0.7V to +0.65V vs. Hg/Hg2SO4) having no influence of redox capacity of the pure lead plate and current to gas evolution was obtained.
For the sake of comparison, a stack (negative electrode) comprising a pure lead plate to which a carbon mixture is not applied, and a separator and a counter electrode comprising lead dioxide, sequentially laminated on both sides of the pure lead plate was used as a comparative sample. The stack was sandwiched between acrylic plates, and fixed such that a pressure of 20 kPa is applied thereto. Charge and discharge were repeated 10 times under the same conditions as above, and cathode potential due to hydrogen evolution initiation at 10th cycle and coulomb amount in a range of −0.7V to +0.65V were obtained. The results are shown in Table 4.
As is apparent from Table 4, when the amount of a volatile component of activated carbon is 36.2% by weight, exceeding 30% by weight, hydrogen overvoltage moves into a noble side, and additionally, the coulomb amount is decreased.
As is apparent from Comparative Test Examples 1 to 3, when activated carbon modified with a functional group, containing a volatile component in a range of 3 to 30% by weight is compounded with a carbon mixture, the resulting carbon mixture is applied to a surface of a negative plate comprising a lead active material-filled plate, and a negative electrode having the carbon mixture coating layer formed thereon is used in a lead-acid storage battery, increase in hydrogen gas evolution is inhibited, battery life is prolonged, and rapid discharge cycle characteristics in PSCO are excellent. Furthermore, use of the negative electrode in industrial fields utilizing a battery, such as hybrid automobiles and windmills, brings about improvement of negative electrode polarity.
The present inventors have further found that in an active material modified with a functional group, specific kind and amount of a surface functional group of activated carbon plays an important role in improving cycle life of a lead-acid storage battery. Samples A to K shown in Table 5 below were prepared by the following methods.
1) Coconut shell activated carbon obtained by subjecting coconut shell type activated carbon to steam activation for 2 hours was used as Sample A.
2) Air oxidation method
The activated carbon of Sample A was surface-treated with an air oxidation method. Specifically, the activated carbon was heated to 350° C. in wet air stream (1 liter/min), and held at the temperature for 1 hour, 3 hours or 5 hours, followed by cooling to room temperature. The activated carbons thus prepared were used as Samples B, C and D, respectively.
3) Solution oxidation method
The activated carbon of Sample A was surface-treated with a solution oxidation method. Specifically, the activated carbon was dipped in an ammonium persulfate aqueous solution having a concentration of 0.3 mol/liter, 1.5 mol/liter, 1.0 mol/liter, 1.2 mol/liter or 2.0 mol/liter, and then allowed to stand for two days and nights, followed by washing with water and drying. Those activated carbons thus obtained were used as Samples E, F, G, H and I, respectively.
4) Heat treatment method
The activated carbon of Sample A was surface-treated with a heat treatment method. Specifically, the activated carbon was heated to 800° C. in a nitrogen atmosphere, and then held at the temperature for 1 hour or 2 hours, followed by cooling to room temperature. The activated carbons thus prepared were used as Samples J and K, respectively.
The amount of the acidic surface functional group in the activation carbons of Samples A to K was measured in the following procedures a), b) and c). The amount of the functional group was measured utilizing the principle that a neutralization reaction occurs between each of three kinds of acidic functional groups, a carboxyl group, a lactone group and a phenolic hydroxyl group, and sodium hydroxide, and the amount of the surface functional group was calculated from the amount of sodium hydroxide consumed in the neutralization reaction.
a) Pre-Treatment
Each of the activated carbons of Samples A to K to be measured was placed in a crucible, and dried in an electric furnace at 300° C. for 3 hours. Each of the samples was cooled to room temperature in a desiccator. Each sample thus treated was used as a measurement sample.
b) Reaction of Carboxyl Group, Lactone Group and Hydroxyl Group
0.1 g of each measurement sample and 50 ml of 0.1M NaOH aqueous solution were placed in a flask, and the flask was applied on a shaker for 2 days. The resulting mixture was then filtered, and the filtrate thus obtained was used as a measurement solution.
c) Quantitative Determination of Acidic Surface Functional Group
20 ml of the measurement solution was sampled, and subjected to back titration with 0.1M HCl aqueous solution. The amount (mmol/g) of a surface functional group was calculated from volume difference to a blank test. The results are shown in Table 5 above.
Specific surface area and average particle size of activated carbons of Samples A to K were measured as follows.
a) Measurement of Specific Surface Area
Specific surface area of the activated carbons of Samples A to K was measured using a nitrogen adsorption method. Specifically, 2.0 g of each measurement sample of Samples A to K having been subjected to the pre-treatment was measured with an automatic specific surface area measuring device (JEMINI 2360, manufactured by Shimadzu Corporation), and a specific surface area (m2/g) was calculated from the BET equation. The results are shown in Table 5.
b) Measurement of Average Particle Size
Average particle size of the activated carbons of Samples A to K was measured using a laser diffraction method. Specifically, the average particle size of 1.0 g of each measurement sample of Samples A to K having been subjected to the pre-treatment of the above was measured with a laser diffraction scattering particle size distribution measuring device (SK Laser Micron Sizer LMS-2000e, manufactured by Seishin Enterprise Co., Ltd.). The results are shown in Table 5 above.
The amount of a surface functional group per unit area of activated carbon was calculated from the measurement results of the amount of an acidic surface functional group per 1 g of activated carbon obtained above and the specific surface area per 1 g of each of activated carbons A to K obtained by the above measurement method of a specific surface area. The results are shown in Table 5 above.
Using each activated carbon of eleven Samples A to K, a hybrid negative plate for a lead-acid storage battery was prepared in the following manner.
0.5 part by weight of an acetylene black powder as a conductive carbon material and 0.75 part by weight (1.5 times the amount of the acetylene black powder) of a barium sulfate powder were added to 100 parts by weight of a negative electrode active material comprising a lead powder comprising lead monoxide produced by a ball mill method as a main component, followed by mixing. Lignin in an amount of 0.2% by weight based on the weight of the negative electrode active material, 3 g of water, and ion-exchanged water in an amount of 10% by weight based on the weight of the negative electrode active material were added to the mixture obtained above, followed by kneading. Diluted sulfuric acid having specific gravity of 1.36 in an amount of 9.5 parts by weight relative to 100 parts by weight of the negative electrode active material was further added to the resulting mixture, followed by kneading. Thus, a negative electrode active material paste having cap density of about 135 g/2 in3 was prepared. The negative electrode active material paste thus prepared was filled in a collecting grid substrate comprising Pb—Ca alloy, followed by aging in the atmosphere of 40° C. and 95% humidity for 24 hours, and then drying. Thus, a plurality of unformed negative plates was produced.
40 parts by weight of each of eleven kinds of activated carbons different from Samples A to K were added to the formulation composition of a carbon mixture paste shown in Table 6 below to prepare eleven kinds of carbon mixture pastes. Each carbon mixture paste was applied to the entire both surfaces of the negative plate excluding lug in an amount of 8% by weight based on the weight of the active material contained in the negative plate in terms of dry weight when the carbon mixture paste was dried, in a thickness of 0.2 mm. The resulting coating film was dried in air at 60° C. for 1 hour, and at the same time, a lead active material was oxidized. Thus, eleven kinds of hybrid negative plates having formed on the surface of each negative plate a porous carbon mixture coating layer having a porosity of 75% were prepared.
10 parts by weight of ion-exchanged water and 10 parts by weight of diluted sulfuric acid having specific gravity of 1.27 were added to 100 parts by weight of lead oxide, followed by kneading, to prepare a paste for a positive electrode. The paste for a positive electrode was filled in a collecting grid substrate comprising Pb—Ca alloy, and aged in the atmosphere of 40° C. and 95% humidity for 24 hours, followed by drying. Thus, a plurality of unformed positive plates was prepared.
Five hybrid negative plates and four positive plates prepared above were alternately laminated on each of eleven kinds of the hybrid negative plates prepared above though fine glass mat separators. Lugs of the same polar plates were welded by COS system. Thus, a plate group was assembled. The plate group was placed in a battery case made of polypropylene in the same manner as in the conventional assembling method of a valve-regulated lead-acid storage battery. The battery case was lidded by heat sealing to seal an opening. Thus, eleven kinds of 2V valve-regulated lead-acid storage batteries A to K having 5-hour rate capacity of 10 Ah in capacity control of positive electrode were assembled. In the insertion of the group, degree of compression of the plate group was adjusted by inserting a spacer between the battery case and the plate group as to be 50 kPa. Sulfuric acid aqueous solution having specific gravity of 1.30 prepared by dissolving 30 g/liter of aluminum sulfate octadeca hydrate in water was poured as an electrolyte in each of the lead-acid storage batteries assembled above. Those batteries were charged at 1 A for 20 hours, and then discharged at 2 A until cell voltage becomes 1.75V. The batteries were again charged at 1 A for 15 hours and then discharged at 2 A until a cell voltage of 1.75V. Thus, eleven kinds of lead-acid storage batteries (cells) A to K having 5-hour rate capacity of 10 Ah were produced.
Each of the lead-acid storage batteries (cells) A to K comprising each of the eleven kinds of the hybrid negative plates was subjected to the following cycle life test by repeating rapid charge and discharge in PSOC in the form of the simulation of running by HEV. Specifically, the test is as follows. Each cell was discharged at 2 A for 1 hour to make PSOC of 80%. Discharging at 50 A for 1 second and charging at 20 A for 1 second were repeated 500 times in the atmosphere of 40° C., and charging at 30 A for 1 second and pausing for 1 second were then repeated 510 times. Those operations were taken as one cycle. This cycle test was repeated, and when discharge voltage of 2V cell reached 0V, it was considered as the end of its life. The results of rapid charge and discharge cycle life test of each of the lead-acid storage batteries are shown in Table 3.
As is apparent from Table 5 and Table 7 above, great change in specific surface area by a surface oxidation treatment is not observed, and change in an average particle size is not substantially observed. It is therefore seen from this fact that the amount of an acidic surface functional group of an activated carbon greatly affects cycle life of a lead-acid storage battery comprising the hybrid negative plate. To compare the amount of an acidic surface functional group of each sample in “per unit area”, a value (μmol/m2) obtained by dividing the amount (mmol/g) of an acidic functional group by a specific surface area (m2/g) was calculated, and the relationship between the value and cycle life of the lead-acid storage batteries A to K each comprising the hybrid negative plate is shown in
As a result of obtaining polynomial approximation of plots excluding data of Sample I having values greatly deviated from the plots of Samples A to K shown in
y=−843.06x2+2754.6x+91.458
R
2=0.9415
wherein x is an amount of an acidic surface functional group, y is cycle life and R2 is coefficient of determination.
The life of the lead-acid storage battery A is 350 cycles. When 500 cycles that are about 1.5 times the 350 cycles is used as a standard of superiority of cycle life and 500 is substituted for y of the above mathematical formulae, the solution obtained is x=0.16 and 3.11. That is to say, when the amount of an acidic surface functional group is 0.16 to 3.11 μmol/m2, the lead-acid storage batteries B to G comprising hybrid negative plates using the activated carbons A to G improve the life to 500 cycles or more.
In the lead-acid storage battery A, the lead-acid batteries B to G, and the lead-acid storage batteries J and K, in which the amount of an acidic surface functional group per unit area is 0.08 to 1.17 μmol/m2, a positive linear relation is established. The reason for this is considered that capacitor capacity is increased in proportion to increase in the amount of a functional group. Charge acceptability of a lead-acid storage battery is improved with increasing capacitor capacity, and this leads to the result of long life.
On the other hand, while capacitor capacity is increased as the amount of an acidic surface functional group per unit area is increased, reduction amount of an electrolyte is increased. Generally, in the cycle life test by repeating rapid charge and discharge in PSOC, a battery comes to the end of its life by deterioration (sulfation) of a negative plate, but when the amount of a functional group is 1.93 μmol/m2 or more, the battery came to the end of its life by electrolyte leakage. Therefore, from the standpoint of capacitor capacity, the larger the amount of a surface functional group of activated carbon, the better. However, from the standpoint of battery life, it was found that too large amount of a surface functional group has an adverse effect to the battery life.
To specifically examine as to what kind of an acidic surface functional group affects the life, activated carbons of Samples L to Q shown in Table 8 below were prepared. Using those Samples, the amount of a surface functional group was quantitatively determined, and properties (specific surface area and average particle size) were measured.
Phenol resin-based activated carbon having been subjected to alkali activation for 1 hour was used as Sample L, coconut shell activated carbons having been subjected to steam activation for 2 hours were used as Samples M to P, and wood activated carbon having been subjected to phosphoric acid activation for 2 hours was used as Sample Q. The amount of each acidic surface functional group of each activated carbon of Samples L to Q was quantitatively determined by the conventional method as described in paragraph 0014 of JP-A 2004-47613. Specifically, 2 g of each activated carbon sample was placed in a 100 ml Erlenmeyer flask, 50 ml of each of N/10 alkali reagents ((a) sodium hydrogen carbonate, (b) sodium carbonate, (c) sodium hydroxide, and (d) sodium ethoxide) was added to the flask, followed by shaking for 24 hours and then filtering. Unreacted alkali reagent was titrated with N/10 hydrochloric acid. Carboxyl group reacts with all of the alkali reagents (a) to (d), lactone group reacts with the alkali reagents (b) to (d), and phenolic hydroxyl group reacts with the alkali reagents (c) and (d). Therefore, the amount of each acidic surface functional group was quantitatively determined by deduction of each titration amount. The results are shown in Table 8.
Specific surface area and average particle size of the activated carbons of Samples L to Q were measured in the same manners as in Comparative Test Example 3. The results are shown in Table 8.
From the measurement results of the amount of a functional group per 1 g of activated carbon obtained above and the specific surface area per 1 g of activated carbon obtained above, the amount of carboxyl group, the amount of lactone group and the amount of phenolic hydroxyl group, per unit area of activated carbon were calculated. The total of carboxyl group, lactone group and phenolic hydroxyl group was considered as the total acid group. The results are shown in Table 8.
Valve-regulated lead-acid storage batteries, that is, storage batteries L to Q shown in Table 9 below, comprising 2V cells having 5-hour rate capacity of 10 Ah were assembled in the same manner as in Comparative Test Example 4, except that activated carbon as a sample differs, followed by preparation of an electrolyte, formation and capacity measurement. Thus, finished batteries were obtained.
Cycle life test was conducted under the same conditions as in Comparative Test Example 4, except that activated carbon as a sample differs. The results are shown in Table 9 above.
To compare the amount of a surface functional group of each sample in “per unit area”, a value (μmol/m2) obtained by dividing the amount (mmol/g) of each functional group by a specific surface area (m2/g) was calculated, and the relationship between the value and cycle life of the lead-acid storage batteries each comprising the hybrid negative plate was examined. In the relationship between the amount of carboxyl group and cycle life, as a result of obtaining linear approximation from each plot as shown in
y=11469x+606.11
R
2=0.9068
wherein x is an amount of carboxyl group, y is cycle life, and R2 is coefficient of determination.
The life of the storage battery A in Table 7 is 350 cycles. When 700 cycles that are 2 times the 350 cycles is used as a standard of superiority of life cycle and 700 is substituted for y in the above mathematical formulae, the solution obtained is x=0.01. That is to say, when the amount of carboxyl group is 0.01 μmol/m2 or more, the lead-acid storage battery comprising the hybrid negative plate can improve the cycle life.
In the relationship between the amount of lactone group and cycle life, as a result of obtaining linear approximation from each plot as shown in
y=10684x+251
R
2=0.9245
wherein x is an amount of lactone group, y is cycle life, and R2 is coefficient of determination.
Similar to the above, when 700 cycles is used as a standard of superiority of life cycle and 700 is substituted for y in the above mathematical formulae, the solution obtained is x=0.04. That is to say, when the amount of lactone group is 0.04 μmol/m2 or more, the lead-acid storage battery comprising the hybrid negative plate can improve the cycle life.
In the relationship between the amount of phenolic hydroxyl group and cycle life, as a result of obtaining linear approximation from each plot as shown in
y=4395.3x+194.87
R
2=0.5791
wherein x is an amount of phenolic hydroxyl group, y is cycle life, and R2 is coefficient of determination.
Similar to the above, when 700 cycles are used as a standard of superiority of life cycle and 700 is substituted for y in the above mathematical formulae, the solution obtained is x=0.11. That is to say, when the amount of phenolic hydroxyl group is 0.14 μmol/m2 or more, the lead-acid storage battery comprising the hybrid negative plate can improve the cycle life.
When the relationship between an amount of each functional group and cycle life is examined, it is apparent from
As is apparent from Comparative Test Examples 4 and 5, a lead-acid storage battery comprising a hybrid negative plate comprising a negative plate comprising a lead active material-filled plate and a carbon mixture coating layer comprising activated carbon modified with a specific acidic surface functional group, formed on the surface of the negative plate has long cycle life and excellent rapid discharge cycle characteristics in PSOC, and is therefore extremely useful for use in industrial fields utilizing a battery, such as hybrid automobiles repeating on-off operations of an engine, and windmills.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2009-196201 | Aug 2009 | JP | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/JP2010/064984 | 8/26/2010 | WO | 00 | 6/19/2012 |
