TWI545831B - Control valve type leaded battery - Google Patents
Control valve type leaded battery Download PDFInfo
- Publication number
- TWI545831B TWI545831B TW103143054A TW103143054A TWI545831B TW I545831 B TWI545831 B TW I545831B TW 103143054 A TW103143054 A TW 103143054A TW 103143054 A TW103143054 A TW 103143054A TW I545831 B TWI545831 B TW I545831B
- Authority
- TW
- Taiwan
- Prior art keywords
- graphite
- control valve
- negative electrode
- mass
- storage battery
- Prior art date
Links
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 78
- 229910002804 graphite Inorganic materials 0.000 claims description 58
- 239000010439 graphite Substances 0.000 claims description 52
- 238000003860 storage Methods 0.000 claims description 42
- 238000010521 absorption reaction Methods 0.000 claims description 39
- 239000002245 particle Substances 0.000 claims description 39
- 239000007773 negative electrode material Substances 0.000 claims description 33
- 239000006229 carbon black Substances 0.000 claims description 17
- 239000006230 acetylene black Substances 0.000 claims description 16
- 239000002253 acid Substances 0.000 claims description 3
- DOIRQSBPFJWKBE-UHFFFAOYSA-N dibutyl phthalate Chemical compound CCCCOC(=O)C1=CC=CC=C1C(=O)OCCCC DOIRQSBPFJWKBE-UHFFFAOYSA-N 0.000 description 68
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 22
- 238000000034 method Methods 0.000 description 14
- 230000000052 comparative effect Effects 0.000 description 10
- 239000000835 fiber Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- 239000007774 positive electrode material Substances 0.000 description 7
- 238000012360 testing method Methods 0.000 description 7
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- -1 polypropylene Polymers 0.000 description 5
- 230000005070 ripening Effects 0.000 description 5
- 229920005552 sodium lignosulfonate Polymers 0.000 description 5
- 229910001128 Sn alloy Inorganic materials 0.000 description 4
- 238000007600 charging Methods 0.000 description 4
- 238000011156 evaluation Methods 0.000 description 4
- 239000006232 furnace black Substances 0.000 description 4
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 4
- 239000005020 polyethylene terephthalate Substances 0.000 description 4
- 229920000139 polyethylene terephthalate Polymers 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000003365 glass fiber Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000003014 reinforcing effect Effects 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 239000003792 electrolyte Substances 0.000 description 2
- 239000008151 electrolyte solution Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000002142 lead-calcium alloy Substances 0.000 description 2
- 229920001955 polyphenylene ether Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920002972 Acrylic fiber Polymers 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- BUGBHKTXTAQXES-UHFFFAOYSA-N Selenium Chemical compound [Se] BUGBHKTXTAQXES-UHFFFAOYSA-N 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- DPDORTBBLUCNJG-UHFFFAOYSA-N calcium tin Chemical compound [Ca].[Sn] DPDORTBBLUCNJG-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000006231 channel black Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- YDEXUEFDPVHGHE-GGMCWBHBSA-L disodium;(2r)-3-(2-hydroxy-3-methoxyphenyl)-2-[2-methoxy-4-(3-sulfonatopropyl)phenoxy]propane-1-sulfonate Chemical compound [Na+].[Na+].COC1=CC=CC(C[C@H](CS([O-])(=O)=O)OC=2C(=CC(CCCS([O-])(=O)=O)=CC=2)OC)=C1O YDEXUEFDPVHGHE-GGMCWBHBSA-L 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000007580 dry-mixing Methods 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000007770 graphite material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000003273 ketjen black Substances 0.000 description 1
- 238000007561 laser diffraction method Methods 0.000 description 1
- 229910000464 lead oxide Inorganic materials 0.000 description 1
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- YEXPOXQUZXUXJW-UHFFFAOYSA-N oxolead Chemical compound [Pb]=O YEXPOXQUZXUXJW-UHFFFAOYSA-N 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000010278 pulse charging Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000000790 scattering method Methods 0.000 description 1
- 229910052711 selenium Inorganic materials 0.000 description 1
- 239000011669 selenium Substances 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 150000003385 sodium Chemical class 0.000 description 1
- 230000019635 sulfation Effects 0.000 description 1
- 238000005670 sulfation reaction Methods 0.000 description 1
- 239000006234 thermal black Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/14—Electrodes for lead-acid accumulators
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/06—Lead-acid accumulators
- H01M10/12—Construction or manufacture
- H01M10/121—Valve regulated lead acid batteries [VRLA]
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M4/62—Selection of inactive substances as ingredients for active masses, e.g. binders, fillers
- H01M4/624—Electric conductive fillers
- H01M4/625—Carbon or graphite
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/02—Electrodes composed of, or comprising, active material
- H01M2004/021—Physical characteristics, e.g. porosity, surface area
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Landscapes
- 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)
Description
本發明係有關在部分充電狀態下使用之控制閥式鉛蓄電池。 The present invention relates to a control valve type lead storage battery for use in a partially charged state.
風力或太陽光發電等蓄電及系統電力的平準化所利用之鉛蓄電池,一般會採用控制閥式鉛蓄電池。該控制閥式鉛蓄電池,總是保持在所謂部分充電狀態(PSOC:Partial State of Charge)之充電不足狀態,且進行大電流的脈衝充放電等,被要求能夠在嚴苛的使用條件下使用。然而,若在PSOC狀態下反覆充放電,那麼負極中放電物質亦即硫酸鉛的結晶會成長、粗大化,而發生喪失可逆性之問題(硫酸化,sulfation)。對此,下述專利文獻1(日本特開2003-123760號公報)中揭示一種技術,係使用在負極活性物質中添加碳黑(乙炔碳黑)而得之鉛蓄電池用負極,來作為在PSOC狀態下使用之鉛蓄電池的負極。 A lead-acid battery used for power storage such as wind power or solar power generation and leveling of system power is generally used as a control valve type lead storage battery. The control valve type lead storage battery is always kept in a state of insufficient charge in a so-called partial state of charge (PSOC), and is subjected to pulse charging and discharging of a large current, and is required to be used under severe use conditions. However, if the charge and discharge are reversed in the PSOC state, the crystal of lead sulfate, which is a discharge material in the negative electrode, grows and coarsens, and the problem of loss of reversibility (sulfation) occurs. In the above-mentioned Patent Document 1 (JP-A-2003-123760), a technique is disclosed in which a negative electrode for a lead storage battery obtained by adding carbon black (acetylene black) to a negative electrode active material is used as the PSOC. The negative electrode of the lead battery used in the state.
〔專利文獻1〕日本特開2003-123760號公報 [Patent Document 1] Japanese Patent Laid-Open Publication No. 2003-123760
然而,專利文獻1記載之鉛蓄電池,係偏向汽車用途,由本發明團隊研討之結果發現,當運用於自然能量的蓄電及系統電力的平準化所利用之鉛蓄電池的情形下,循環特性並不足夠。 However, the lead storage battery described in Patent Document 1 is biased toward automobile use. As a result of research by the team of the present invention, it has been found that the cycle characteristics are not sufficient in the case of a lead storage battery used for the storage of natural energy and the leveling of system power. .
本發明係有鑑於上述事態而研發,目的在於針對在部分充電狀態下運用之控制閥式鉛蓄電池,提供一種循環特性優良之控制閥式鉛蓄電池。 The present invention has been made in view of the above circumstances, and aims to provide a control valve type lead storage battery excellent in cycle characteristics for a control valve type lead storage battery that is used in a partially charged state.
本發明作為改良對象之控制閥式鉛蓄電池,為具備於負極活性物質中含有碳黑的負極板之控制閥式鉛蓄電池。負極活性物質中,除碳黑外還含有石墨。本發明中使用之石墨,係平均粒徑為90μm以下,且DBP吸油量為55ml/100g以上之石墨。 The control valve type lead storage battery to be improved according to the present invention is a control valve type lead storage battery including a negative electrode plate containing carbon black in a negative electrode active material. The negative electrode active material contains graphite in addition to carbon black. The graphite used in the present invention is graphite having an average particle diameter of 90 μm or less and a DBP oil absorption of 55 ml/100 g or more.
此處,「平均粒徑」意指藉由雷射繞射/散射法測定之體積基準的累積分布為50%之粒子徑(D50)。此外,「IDBP吸油量」,為藉由JISK-6221(1982)記載之吸油量B法(刮勺拌和法)求出之吸油量。另,石墨的DBP吸油量高,一般而言表示石墨的結晶性高。 Here, the "average particle diameter" means a particle diameter (D50) in which the cumulative distribution of the volume basis measured by the laser diffraction/scattering method is 50%. In addition, the "IDBP oil absorption amount" is an oil absorption amount obtained by the oil absorption amount B method (squeegee mixing method) described in JIS K-6221 (1982). Further, graphite has a high DBP oil absorption, and generally indicates that graphite has high crystallinity.
若將具有這樣的平均粒徑及DBP吸油量之石墨與碳 黑一起添加至負極活性物質,則即使是在PSOC狀態下使用之鉛蓄電池之情形下,仍會維持初始電容而提升循環特性。也就是說,具備使用了負極活性物質之負極板,而該負極活性物質同時含有平均粒徑小且結晶性高(層狀構造未被破壞)的石墨、以及碳黑,藉此便能獲得顯現出比以往更高的循環特性之控制閥式鉛蓄電池。 If graphite and carbon have such average particle size and DBP oil absorption When black is added to the negative electrode active material, even in the case of a lead storage battery used in the PSOC state, the initial capacitance is maintained and the cycle characteristics are improved. In other words, a negative electrode plate using a negative electrode active material is provided, and the negative electrode active material contains graphite having a small average particle diameter and high crystallinity (the layered structure is not destroyed), and carbon black, thereby obtaining appearance. A control valve type lead storage battery with higher cycle characteristics than ever before.
另,若為平均粒徑小且結晶性高之石墨,則石墨的平均粒徑下限值及DBP吸油量上限值並無限定。但,考量石墨材料的可取得性,則料想石墨的平均粒徑下限值為1μm左右、石墨的DBP吸油量上限值為300ml/100g左右。 Further, in the case of graphite having a small average particle diameter and high crystallinity, the upper limit of the average particle diameter of graphite and the upper limit of the DBP oil absorption amount are not limited. However, considering the availability of the graphite material, it is expected that the lower limit of the average particle diameter of graphite is about 1 μm, and the upper limit of the DBP oil absorption of graphite is about 300 ml/100 g.
添加於負極活性物質之石墨,較佳是添加平均粒徑為1μm~60μm,且DBP吸油量為65ml/100g以上之石墨。若使用顯現出這樣數值範圍的平均粒徑及DBP吸油量之石墨,則不僅循環特性會提升,亦能提升初始電容。 The graphite to be added to the negative electrode active material is preferably graphite having an average particle diameter of 1 μm to 60 μm and a DBP oil absorption of 65 ml/100 g or more. When graphite having an average particle diameter and DBP oil absorption in such a numerical range is used, not only the cycle characteristics are improved, but also the initial capacitance can be improved.
此外,石墨更佳是平均粒徑為1μm~20μm,且DBP吸油量為85ml/100g以上。若使用具有這樣數值範圍的平均粒徑及DBP吸油量之石墨,則初始電容會維持或提升,同時循環特性會顯著提升。 Further, it is more preferable that the graphite has an average particle diameter of from 1 μm to 20 μm and a DBP oil absorption of 85 ml/100 g or more. If graphite having an average particle diameter and DBP oil absorption in such a numerical range is used, the initial capacitance is maintained or increased, and the cycle characteristics are remarkably improved.
此外,石墨的含有量,較佳是相對於負極活性物質100質量%為0.5~3.0質量%。若將石墨的含有量調整成這樣的數值範圍,則能確實獲得初始電容與循環特性均提升之控制閥式鉛蓄電池。 Further, the content of graphite is preferably 0.5 to 3.0% by mass based on 100% by mass of the negative electrode active material. When the content of graphite is adjusted to such a numerical range, a control valve type lead storage battery in which initial capacitance and cycle characteristics are improved can be surely obtained.
更佳是,石墨的含有量,相對於負極活性物質100質 量%為1.0~3.0質量%。若將石墨的含有量調整成這樣的數值範圍,則能確實獲得初始電容維持或提升,同時循環特性顯著提升之控制閥式鉛蓄電池。 More preferably, the content of graphite is relative to the negative electrode active material 100. The amount % is 1.0 to 3.0% by mass. When the content of graphite is adjusted to such a numerical range, it is possible to surely obtain a control valve type lead storage battery in which the initial capacitance is maintained or increased while the cycle characteristics are remarkably improved.
另一方面,碳黑的含有量,較佳是調整成相對於負極活性物質100質量%為0.3~3.0質量%。若將碳黑的含有量調整成這樣的數值範圍,則即使石墨的含有量相對較少的情形下,仍能獲得初始電容與循環特性均提升之控制閥式鉛蓄電池。 On the other hand, the content of the carbon black is preferably adjusted to be 0.3 to 3.0% by mass based on 100% by mass of the negative electrode active material. When the content of carbon black is adjusted to such a numerical range, even if the content of graphite is relatively small, a control valve type lead storage battery in which both initial capacitance and cycle characteristics are improved can be obtained.
更佳是,碳黑的含有量,調整成相對於負極活性物質100質量%為1.5~3.0質量%。若將碳黑的含有量調整成這樣的數值範圍,則即使石墨的含有量相對較少的情形下,仍能獲得初始電容維持或提升,同時循環特性顯著提升之控制閥式鉛蓄電池。 More preferably, the content of the carbon black is adjusted to be 1.5 to 3.0% by mass based on 100% by mass of the negative electrode active material. When the content of the carbon black is adjusted to such a numerical range, even if the content of the graphite is relatively small, a control valve type lead storage battery in which the initial capacitance is maintained or increased and the cycle characteristics are remarkably improved can be obtained.
另,添加於負極活性物質之碳黑,可舉出乙炔碳黑、爐黑(furnace black)、槽黑(channel black)、熱碳黑(thermal black)、科琴碳黑(Ketjen black)等。其中又以使用乙炔碳黑,相較於使用乙炔碳黑以外的碳黑之情形,能夠提高循環特性。 Further, examples of the carbon black added to the negative electrode active material include acetylene black, furnace black, channel black, thermal black, and Ketjen black. Further, in the case where acetylene black is used, the cycle characteristics can be improved as compared with the case of carbon black other than acetylene black.
以下,詳細說明本發明之實施形態。本例之控制閥式鉛蓄電池,例如能夠依以下方式製作。 Hereinafter, embodiments of the present invention will be described in detail. The control valve type lead storage battery of this example can be produced, for example, in the following manner.
首先,負極活性物質,是對於以一氧化鉛為主成分之鉛粉,至少添加碳黑(乙炔碳黑)、及平均粒徑為90μm以下且DBP吸油量為55ml/100g以上之石墨。此外,視必要備妥添加硫酸鋇、補強用短纖維(丙烯酸纖維、聚丙烯纖維、聚對苯二甲酸乙二酯(PET)纖維等)等並混練而成之混合物。將該混合物加入水及木質素磺酸鈉(sodium ligninsulfonate)予以混合,更加入稀硫酸而製作出負極活性物質膏。 First, the negative electrode active material is a graphite powder containing at least carbon black (acetylene black) and a graphite powder having an average particle diameter of 90 μm or less and a DBP oil absorption of 55 ml/100 g or more. In addition, a mixture of barium sulfate, reinforcing short fibers (acrylic fiber, polypropylene fiber, polyethylene terephthalate (PET) fiber, etc.) and the like may be added as needed. The mixture was added to water and sodium ligninsulfonate and mixed, and dilute sulfuric acid was further added to prepare a negative electrode active material paste.
作為碳黑而添加之乙炔碳黑的含有量,由至少維持初始電容同時提升循環特性之觀點看來,較佳是相對於負極活性物質100質量%為0.1~5.0質量%。此外,若考量不僅提升循環特性還要提升初始電容,則較佳是相對於負極活性物質100質量%為0.1~3.0質量%。又,為了提升初始電容同時獲得高循環特性,較佳是相對於負極活性物質100質量%為1.5~3.0質量%。 The content of the acetylene black to be added as the carbon black is preferably from 0.1 to 5.0% by mass based on 100% by mass of the negative electrode active material from the viewpoint of maintaining at least the initial capacitance and improving the cycle characteristics. Further, in consideration of not only improving the cycle characteristics but also increasing the initial capacitance, it is preferably 0.1 to 3.0% by mass based on 100% by mass of the negative electrode active material. Moreover, in order to improve the initial capacitance and obtain high cycle characteristics, it is preferably 1.5 to 3.0% by mass based on 100% by mass of the negative electrode active material.
石墨的含有量,若考量至少維持初始電容同時提升循環特性,可相對於負極活性物質100質量%訂為0.5~5質量%。此外,若考量不僅提升循環特性還要提升初始電容,則較佳是相對於負極活性物質100質量%為0.5~3.0質量%。又,為了提升初始電容同時獲得高循環特性,更佳是相對於負極活性物質100質量%為1.0~3.0質量%。 The content of the graphite may be 0.5 to 5% by mass based on 100% by mass of the negative electrode active material, in consideration of at least maintaining the initial capacitance and improving the cycle characteristics. Further, in consideration of not only improving the cycle characteristics but also increasing the initial capacitance, it is preferably 0.5 to 3.0% by mass based on 100% by mass of the negative electrode active material. Moreover, in order to improve the initial capacitance and obtain high cycle characteristics, it is more preferably 1.0 to 3.0% by mass based on 100% by mass of the negative electrode active material.
另,石墨的DBP吸油量能夠藉由上述刮勺拌和法求出。 Further, the DBP oil absorption of graphite can be obtained by the above-described spatula mixing method.
石墨的平均粒徑,由至少維持初始電容同時提升循環 特性的觀點看來,可如上述般訂為90μm以下。此外,由不僅提升循環特性還要提升初始電容的觀點看來,較佳為1μm~60μm,若由提升初始電容同時還進一步提升循環特性的觀點看來,更佳為1μm~20μm。另,平均粒徑係以上述粒子徑(D50)來求出。 The average particle size of graphite, which is maintained by at least maintaining the initial capacitance From the viewpoint of characteristics, it can be set to 90 μm or less as described above. Further, from the viewpoint of not only improving the cycle characteristics but also increasing the initial capacitance, it is preferably from 1 μm to 60 μm, and more preferably from 1 μm to 20 μm from the viewpoint of improving the initial capacitance while further improving the cycle characteristics. Further, the average particle diameter is determined by the above particle diameter (D50).
此外,石墨的DBP吸油量,由至少維持初始電容同時提升循環特性的觀點看來,可如上述般訂為55ml/100g以上。此外,由不僅提升循環特性還要提升初始電容的觀點看來,較佳為65ml/100g以上,若由提升初始電容同時還進一步提升循環特性的觀點看來,更佳為85ml/100g以上。另,DBP吸油量,其上限並無限制,但由實用性觀點看來認為以500ml/100g以下為佳,實務上只要300ml/100g以下即可。 Further, the DBP oil absorption of graphite can be set to 55 ml/100 g or more as described above from the viewpoint of maintaining at least the initial capacitance while improving the cycle characteristics. Further, from the viewpoint of not only improving the cycle characteristics but also increasing the initial capacitance, it is preferably 65 ml/100 g or more, and more preferably 85 ml/100 g or more from the viewpoint of improving the initial capacitance while further improving the cycle characteristics. In addition, the upper limit of the DBP oil absorption is not limited, but it is considered to be 500 ml/100 g or less from the viewpoint of practicality, and it is only required to be 300 ml/100 g or less in practice.
此外,為了更加提升放電特性,亦可添加木質素磺酸鈉。當含有木質素磺酸鈉的情形下,其含有量相對於負極活性物質100質量%為0.05~1質量%較佳、0.1~0.8質量%更佳、0.2~0.6質量%又更佳。 In addition, in order to further improve the discharge characteristics, sodium lignosulfonate may also be added. When sodium lignosulfonate is contained, the content thereof is preferably 0.05 to 1% by mass, more preferably 0.1 to 0.8% by mass, more preferably 0.2 to 0.6% by mass, based on 100% by mass of the negative electrode active material.
此外,當含有補強用短纖維的情形下,其含有量相對於負極活性物質100質量%為0.01~0.3質量%較佳、0.02~0.1質量%更佳。 In addition, when the reinforcing short fibers are contained, the content thereof is preferably 0.01 to 0.3% by mass, more preferably 0.02 to 0.1% by mass, based on 100% by mass of the negative electrode active material.
當使用硫酸鋇的情形下,其含有量相對於負極活性物質100質量%訂為0.01~2質量%較佳、訂為0.1~1.5質量%更佳。 In the case of using barium sulfate, the content thereof is preferably 0.01 to 2% by mass, more preferably 0.1 to 1.5% by mass, based on 100% by mass of the negative electrode active material.
接下來,將如上述般製作出之負極活性物質膏充填於 集電體格子(grid),熟成後使其乾燥,製作出尚未化成(formation)之負極板。 Next, the negative electrode active material paste prepared as described above is filled in The current collector grid is dried and dried to produce a negative electrode plate that has not yet been formed.
作為集電體格子,能夠使用由鉛-鈣-錫合金,鉛-鈣合金,或在它們當中微量添加砷、硒、銀、鉍而成之鉛-鈣-錫系合金,鉛-鈣系合金等所構成之物。 As the current collector lattice, a lead-calcium-tin alloy, a lead-calcium alloy, which is a lead-calcium-tin alloy, a lead-calcium alloy, or a trace amount of arsenic, selenium, silver, or antimony added thereto may be used. Etc.
熟成條件,較佳為在溫度35~85℃、濕度50~90%環境下訂為40~60小時。乾燥條件,較佳為在溫度50~80℃下訂為15~30小時。 The ripening condition is preferably 40 to 60 hours in an environment of a temperature of 35 to 85 ° C and a humidity of 50 to 90%. The drying condition is preferably set at 15 to 30 hours at a temperature of 50 to 80 °C.
正極板,例如能夠藉由下述方法獲得。首先,對於以一氧化鉛為主成分之鉛粉,加入補強用短纖維後,加入水及稀硫酸。將其混練製作出正極活性物質膏。當製作正極活性物質膏時,亦可加入鉛丹(Pb3O4)。將該正極活性物質膏充填於集電體(集電體格子等)後,進行熟成及乾燥,藉由獲得尚未化成之正極。正極活性物質膏中,補強用短纖維的含有量,以正極活性物質的全質量為基準,較佳為0.005~0.3質量%。集電體格子的種類、熟成條件、乾燥條件,與負極之情形幾乎相同。 The positive electrode plate can be obtained, for example, by the following method. First, for the lead powder containing lead oxide as a main component, after adding short fibers for reinforcement, water and dilute sulfuric acid are added. This was kneaded to prepare a positive electrode active material paste. When preparing a positive active material paste, lead dan (Pb 3 O 4 ) may also be added. This positive electrode active material paste is filled in a current collector (such as a current collector lattice), and then matured and dried to obtain a positive electrode that has not yet been formed. In the positive electrode active material paste, the content of the reinforcing short fibers is preferably 0.005 to 0.3% by mass based on the total mass of the positive electrode active material. The type, ripening conditions, and drying conditions of the current collector lattice are almost the same as those of the negative electrode.
組裝工程中,例如將如上述般製作出之負極及正極,隔著支承板(retainer,或隔板separator)而層積,並以連接片(strap)連結同極性的極板彼此而得到極板群。將 該極板群配置於電解槽內而製作出尚未化成電池。接下來,將稀硫酸倒入尚未化成電池,進行化成處理。接著,暫且將稀硫酸抽乾後,再倒入電解液(稀硫酸),藉此獲得鉛蓄電池。稀硫酸的比重(20℃換算)較佳為1.25~1.35。電解槽的材質並無特別限制,具體而言能夠使用聚丙烯、ABS、變性PPE(聚苯醚)等。 In the assembly process, for example, the negative electrode and the positive electrode produced as described above are laminated via a support plate or a separator, and the plates of the same polarity are connected to each other by a strap to obtain a plate. group. will The electrode group is placed in an electrolytic cell to produce a battery that has not yet been formed. Next, the dilute sulfuric acid is poured into a battery that has not yet been turned into a chemical conversion treatment. Then, the dilute sulfuric acid is drained and then poured into an electrolytic solution (dilute sulfuric acid) to obtain a lead storage battery. The specific gravity (in terms of 20 ° C) of dilute sulfuric acid is preferably 1.25 to 1.35. The material of the electrolytic cell is not particularly limited, and specifically, polypropylene, ABS, denatured PPE (polyphenylene ether), or the like can be used.
蓋體,如先前所述只要是將電解槽的開口部予以閉塞之物,則無特別限制,關於材質則能使用和電解槽相同者,亦可為相異者。但,為了避免加熱時的變形導致發生蓋體脫落,較佳是使用熱膨脹係數相同程度者。 The lid body is not particularly limited as long as it is an opening that closes the opening of the electrolytic cell, and the material may be the same as the electrolytic cell or may be different. However, in order to prevent the cover from falling off due to deformation during heating, it is preferable to use the same degree of thermal expansion coefficient.
控制閥,係用來將充電時產生之氧氣當中無法被負極的氣體吸收反應吸收殆盡之剩餘氣體排出至電解槽外。材質為耐化學性(耐酸性、耐矽油(silicone oil))、耐磨耗性、耐熱性優良之材質,具體而言較佳是使用氟橡膠。 The control valve is used to discharge the remaining gas which is not absorbed by the gas absorption reaction of the negative electrode among the oxygen generated during charging to the outside of the electrolytic cell. The material is a material excellent in chemical resistance (acid resistance, silicone oil resistance), abrasion resistance, and heat resistance, and specifically, a fluorine rubber is preferably used.
支承板(隔板)的材質,可舉出玻璃纖維等。另,化成條件、及稀硫酸的比重,能夠因應電極尺寸來調整。此外,化成處理並不限於在組裝工程中實施,亦可在電極製造工程中實施。 The material of the support plate (separator) may be glass fiber or the like. Further, the chemical conversion conditions and the specific gravity of the dilute sulfuric acid can be adjusted in accordance with the electrode size. Further, the chemical conversion treatment is not limited to being carried out in an assembly process, and may be carried out in an electrode manufacturing process.
以下,具體說明本例中使用之實施例。 Hereinafter, the embodiment used in this example will be specifically described.
對於鉛粉100質量%,添加乙炔碳黑(商品名:DENKA BLACK,電氣化學工業公司製)1.5質量%、石墨(商品名:UP-5,日本石墨工業公司製,平均粒徑:5μm,DBP吸油量:220ml/100g)2質量%、硫酸鋇1質量%、聚對苯二甲酸乙二酯纖維(PET纖維)0.03質量%、木質素磺酸鈉(商品名:VANILLEX N、日本製紙公司製)0.5質量%後,予以乾式混合。接下來,一面加入稀硫酸(比重1.26/20℃換算)及水一面混練,製作出負極活性物質膏。另一方面,將鉛-鈣-錫合金予以熔融、鑄造,製作出長:131.0mm、寬:116.0mm、厚:2.5mm的集電體格子。將準備好的負極活性物質膏充填於該集電體格子後,依以下熟成、乾燥條件製作出負極板。 For the lead powder, 100% by mass, 1.5% by mass of acetylene black (trade name: DENKA BLACK, manufactured by Denki Kagaku Kogyo Co., Ltd.) and graphite (trade name: UP-5, manufactured by Nippon Graphite Co., Ltd., average particle size: 5 μm, DBP) Oil absorption: 220 ml/100 g) 2% by mass, barium sulfate 1% by mass, polyethylene terephthalate fiber (PET fiber) 0.03 mass%, sodium lignosulfonate (trade name: VANILLEX N, manufactured by Nippon Paper Co., Ltd. After 0.5% by mass, it was dry-mixed. Next, while adding dilute sulfuric acid (specific gravity: 1.26/20 ° C conversion) and water, the negative electrode active material paste was prepared. On the other hand, a lead-calcium-tin alloy was melted and cast to prepare a current collector lattice having a length of 131.0 mm, a width of 116.0 mm, and a thickness of 2.5 mm. After the prepared negative electrode active material paste was filled in the current collector grid, a negative electrode plate was produced under the following aging and drying conditions.
熟成條件…溫度:40℃、濕度:98%、時間:40小時 Ripening conditions... Temperature: 40 ° C, humidity: 98%, time: 40 hours
乾燥條件…溫度:60℃、時間:24小時 Drying conditions... Temperature: 60 ° C, Time: 24 hours
石墨的吸油量,是藉由刮勺拌和法,將鄰苯二甲酸二丁酯(dibutyl phthalate;DBP)少量少量地滴下至石墨,並測定石墨試料全體結塊時之DBP滴下量。此外,石墨的平均粒徑(D50),係依JIS R1629記載之方法測定。 The oil absorption of graphite is obtained by dropping a small amount of dibutyl phthalate (DBP) to graphite by a spatula mixing method, and measuring the amount of DBP dripping when the graphite sample is agglomerated. Further, the average particle diameter (D50) of graphite was measured by the method described in JIS R1629.
以鉛粉的全質量為基準,對鉛粉添加由0.15質量%的聚乙烯纖維所構成之短纖(cut fiber)、6質量%的鉛丹後,予以乾式混合。接下來,加入稀硫酸(比重1.26/20℃換算)及水並混練,製作出正極活性物質膏。將鉛- 鈣-錫合金予以熔融、鑄造,製作出長:130.0mm、寬:115.0mm、厚:4.05mm的集電體格子。將正極活性物質膏充填於集電體格子後,依以下熟成、乾燥條件製作出正極板。 On the basis of the total mass of the lead powder, a cut fiber composed of 0.15 mass% of polyethylene fibers and a lead mass of 6 mass% were added to the lead powder, followed by dry mixing. Next, dilute sulfuric acid (specific gravity: 1.26/20 ° C conversion) and water were added and kneaded to prepare a positive electrode active material paste. Lead - The calcium-tin alloy was melted and cast to produce a current collector lattice having a length of 130.0 mm, a width of 115.0 mm, and a thickness of 4.05 mm. After the positive electrode active material paste was filled in the current collector grid, the positive electrode plate was produced under the following aging and drying conditions.
熟成條件1…溫度:80℃、濕度:98%、時間:10小時 Ripening conditions 1... Temperature: 80 ° C, humidity: 98%, time: 10 hours
熟成條件2…溫度:65℃、濕度:75%、時間:11小時 Ripening condition 2... Temperature: 65 ° C, humidity: 75%, time: 11 hours
乾燥條件…溫度:60℃、時間:24小時 Drying conditions... Temperature: 60 ° C, Time: 24 hours
以尚未化成的負極板及尚未化成的正極板交互層積之方式,隔著玻璃纖維製的支承板(控制閥式鉛蓄電池用的隔板)層積3片尚未化成負極板及2片尚未化成正極板後,使同極性極板的耳部彼此以連接片連結,製作出極板群。將極板群插入至電解槽,注入比重為1.050(20℃)的稀硫酸電解液,以理論電容的250%的供電量、化成時間40小時、周圍溫度40℃之條件予以化成。化成後將電解液排出,隔著玻璃纖維製的支承板層積1片已化成負極板及2片已化成正極板後,注入規定量的電解液(比重1.275稀硫酸),安裝安全閥,組裝成控制閥式鉛蓄電池。 A laminated plate made of glass fiber (a separator for a control valve type lead storage battery) is laminated on a support plate (a separator for a control valve type lead storage battery) which is not yet formed, and has not been formed into a negative electrode plate and two pieces have not yet been formed. After the positive electrode plate, the ear portions of the same polarity plate were connected to each other by a connecting piece to form an electrode group. The electrode group was inserted into an electrolytic cell, and a dilute sulfuric acid electrolyte having a specific gravity of 1.050 (20 ° C) was injected, and was formed under the conditions of a power supply amount of 250% of the theoretical capacity, a formation time of 40 hours, and an ambient temperature of 40 °C. After the chemical conversion, the electrolyte is discharged, and one sheet of the negative electrode plate and two sheets of the positive electrode plate are laminated through a support plate made of glass fiber, and then a predetermined amount of electrolyte solution (specific gravity: 1.275 dilute sulfuric acid) is injected, and a safety valve is attached and assembled. Into the control valve type lead storage battery.
除了將負極板換為表1所示材料及組成以外,如同實施例1般得到控制閥式鉛蓄電池。 A control valve type lead storage battery was obtained as in Example 1 except that the negative electrode plate was changed to the material and composition shown in Table 1.
針對上述控制閥式鉛蓄電池,依下述方式測定電池性能(初始電容及循環特性)。將比較例1的初始電容及循環特性之測定結果各自訂為100,而相對評估實施例的各特性。結果如表1所示。 For the above-described control valve type lead storage battery, battery performance (initial capacitance and cycle characteristics) was measured in the following manner. The measurement results of the initial capacitance and the cycle characteristics of Comparative Example 1 were each set to 100, and the respective characteristics of the examples were evaluated. The results are shown in Table 1.
對於上述控制閥式鉛蓄電池,依以下(a)~(d)手續實施初始電容試驗,評估電池性能。另,該試驗,是在控管成25℃之環境下進行。 For the above-mentioned control valve type lead storage battery, the initial capacitance test was carried out in accordance with the following procedures (a) to (d) to evaluate the battery performance. In addition, the test was carried out under the control of 25 ° C.
將電池的10小時率電容訂為4Ah,依以下手續進行試驗。 The battery's 10-hour capacity was set to 4 Ah, and the test was carried out according to the following procedures.
(a)以0.4A、終止電壓(final voltage)1.80V放電 (a) Discharge at 0.4A, final voltage 1.80V
(b)以0.4A、控制電壓(control voltage)2.42V充電24小時 (b) Charging for 24 hours with 0.4A and control voltage of 2.42V
(c)歇息24小時以上 (c) rest for more than 24 hours
(d)反覆上述(a)~(c)手續2次。 (d) Repeat the above procedures (a) to (c) twice.
將鉛蓄電池的第2次的放電容量訂為初始電容。初始電容的評估,係依以下基準進行。 The second discharge capacity of the lead storage battery is set as the initial capacitance. The initial capacitance is evaluated on the basis of the following criteria.
○:初始電容提升了(初始電容超過100未滿120之情形) ○: The initial capacitance is increased (in case the initial capacitance exceeds 100 and less than 120)
△:初始電容維持不變(初始電容95以上100以下之情形) △: The initial capacitance remains unchanged (in case of initial capacitance of 95 or more and 100 or less)
×:初始電容減少了(初始電容未滿95之情形) ×: The initial capacitance is reduced (in case the initial capacitance is less than 95)
對於上述控制閥式鉛蓄電池,依以下(e)~(h)手續實施PSOC循環試驗予以評估。另,該試驗,是在控管成25℃之環境下進行。 For the above-mentioned control valve type lead storage battery, the PSOC cycle test is carried out in accordance with the following procedures (e) to (h) for evaluation. In addition, the test was carried out under the control of 25 ° C.
將電池的10小時率電容訂為4Ah,依以下手續進行試驗。 The battery's 10-hour capacity was set to 4 Ah, and the test was carried out according to the following procedures.
(e)以0.4A放電9小時 (e) discharge at 0.4A for 9 hours
(f)以2.0A充電1小時 (f) charging at 2.0A for 1 hour
(g)以1.6A充電1.25小時 (g) charging 1.25 hours at 1.6A
(h)反覆上述(e)~(g)手續,每當經過100循環測定10小時率的放電容量。 (h) Repeat the above steps (e) to (g), and measure the discharge capacity at a rate of 10 hours every 100 cycles.
將鉛蓄電池的放電容量達到初始電容比70%時的循環數,評估成為PSOC壽命循環特性。循環特性的評估,係依以下基準進行。 The number of cycles when the discharge capacity of the lead storage battery reaches 70% of the initial capacitance ratio is evaluated as the PSOC life cycle characteristic. The evaluation of the cycle characteristics was carried out on the basis of the following criteria.
◎:循環特性顯著提升了(循環特性為130以上之情形) ◎: The cycle characteristics are significantly improved (when the cycle characteristics are 130 or more)
○:循環特性維持不變或提升了(循環特性為100以上未滿130之情形) ○: The cycle characteristics remain unchanged or increased (when the cycle characteristics are 100 or more and less than 130)
×:循環特性減少了(循環特性未滿100之情形) ×: The cycle characteristics are reduced (when the cycle characteristics are less than 100)
由這樣評估出來的初始電容及循環特性,綜合性地評估控制閥式鉛蓄電池的電池性能。另,綜合評估係依以下基準進行。 From the initial capacitance and cycle characteristics thus evaluated, the battery performance of the control valve type lead storage battery was comprehensively evaluated. In addition, the comprehensive evaluation is based on the following criteria.
◎:初始電容維持不變或提升,循環特性顯著提升了(初始電容超過100,且循環特性為130以上之情形) ◎: The initial capacitance remains unchanged or increased, and the cycle characteristics are significantly improved (initial capacitance exceeds 100, and the cycle characteristics are above 130)
●:初始電容、循環特性均提升了(初始電容超過100,且循環特性超過100未滿130之情形) ●: The initial capacitance and cycle characteristics are improved (initial capacitance exceeds 100, and the cycle characteristics exceed 100 and less than 130)
○:初始電容維持不變而循環特性提升了(初始電容95以上100以下,且循環特性超過100未滿130之情形) ○: The initial capacitance is maintained and the cycle characteristics are improved (initial capacitance 95 or more and 100 or less, and the cycle characteristics exceed 100 and less than 130)
×:初始電容、循環特性的至少其中一者降低(初始電容未滿95之情形、或循環特性為100以下之情形) ×: At least one of the initial capacitance and the cycle characteristic is lowered (in the case where the initial capacitance is less than 95 or the cycle characteristic is 100 or less)
另,表1中各材料的詳細如下所述。 In addition, the details of each material in Table 1 are as follows.
UP-5:DBP吸油量220ml/100g、平均粒徑(D50)5μm之石墨(日本石墨工業公司製)、UP-10:DBP吸油量180ml/100g、平均粒徑(D50)10μm之石墨(日本石墨工業公司製)、SP-20:DBP吸油量90ml/100g、平均粒徑(D50)12μm之石墨(日本石墨工業公司製)、ACB150:DBP吸油量75ml/100g、平均粒徑(D50)50μm之石墨(日本石墨工業公司製)、ACB100:DBP吸油量55ml/100g、平均粒徑(D50)80μm之石墨(日本石墨工業公司製)、ACB100(分級):DBP吸油量50ml/100g、平均粒徑(D50)100μm之石墨(發明者將ACB100分級,增大ACB100的平均粒徑而成者)、ACB50:DBP吸油量40ml/100g、平均粒徑(D50)300μm之石墨(日本石墨工業公司製)、DENKA BLACK:乙炔碳黑(電氣化學工業公司製)、VULCAN XC72:爐黑(furnace black)(CABOT公司製)、PEARLLEX DP:高純度變性木質素磺酸鈉(日本製紙公司製)、VANILLEX N:高純度部分脫磺酸基(desulphation)木質素磺酸鈉(日本製紙公司製)。 UP-5: graphite with a DBP oil absorption of 220 ml/100 g, an average particle diameter (D50) of 5 μm (manufactured by Nippon Graphite Co., Ltd.), UP-10: DBP oil absorption of 180 ml/100 g, and an average particle diameter (D50) of 10 μm of graphite (Japan) Graphite Industry Co., Ltd., SP-20: DBP oil absorption: 90ml/100g, average particle size (D50) 12μm graphite (manufactured by Nippon Graphite Co., Ltd.), ACB150: DBP oil absorption: 75ml/100g, average particle size (D50) 50μm Graphite (manufactured by Nippon Graphite Co., Ltd.), ACB100: DBP oil absorption 55 ml/100 g, average particle size (D50) 80 μm graphite (manufactured by Nippon Graphite Co., Ltd.), ACB100 (classification): DBP oil absorption 50 ml/100 g, average particle Graphite (D50) 100 μm graphite (inventors classified ACB100 to increase the average particle size of ACB100), ACB50: DBP oil absorption 40 ml/100 g, and average particle diameter (D50) 300 μm graphite (manufactured by Nippon Graphite Co., Ltd.) DENKA BLACK: acetylene black (manufactured by Electric Chemical Industry Co., Ltd.), VULCAN XC72: furnace black (manufactured by CABOT Co., Ltd.), PEARLLEX DP: high-purity modified sodium lignosulfonate (manufactured by Nippon Paper Industries Co., Ltd.), VANILLEX N: High-purity partial desulphation sodium lignosulfonate (manufactured by Nippon Paper Industries Co., Ltd.).
由表1可知,若以比較例1為基準,則實施例1~5(平均粒徑:5~80μm、DBP吸油量:55~220ml/100g)中,初始電容維持不變或提升且循環特性提升。其中,實施例1~4(平均粒徑:5~50μm、DBP吸油量:75~220ml/100g)中,可知不僅循環特性提升,初始電容亦提升。又,實施例1~3(平均粒徑:5~12μm、DBP吸油量:90~220ml/100g)中,可知初始電容提升的同時,特性顯著提升(任一者之循環特性均為130以上)。 As can be seen from Table 1, in the examples 1 to 5 (average particle diameter: 5 to 80 μm, DBP oil absorption: 55 to 220 ml/100 g), the initial capacitance was maintained or increased and the cycle characteristics were obtained based on Comparative Example 1. Upgrade. Among them, in Examples 1 to 4 (average particle diameter: 5 to 50 μm, DBP oil absorption: 75 to 220 ml/100 g), it was found that not only the cycle characteristics were improved but also the initial capacitance was also improved. Further, in Examples 1 to 3 (average particle diameter: 5 to 12 μm, DBP oil absorption: 90 to 220 ml/100 g), it was found that the initial capacitance was improved and the characteristics were remarkably improved (any of the cycle characteristics were 130 or more). .
另,比較例2(平均粒徑、DBP吸油量均未滿本發明條件之情形)中,初始電容降低了(初始電容未滿95)。此外,比較例3(DBP吸油量雖滿足本發明條件,但平均粒徑未滿本發明條件之情形)中,初始電容亦降低了(初始電容未滿95)。 Further, in Comparative Example 2 (in the case where the average particle diameter and the DBP oil absorption amount were all less than the conditions of the present invention), the initial capacitance was lowered (the initial capacitance was less than 95). Further, in Comparative Example 3 (when the DBP oil absorption amount satisfies the conditions of the present invention, but the average particle diameter is less than the condition of the present invention), the initial capacitance is also lowered (the initial capacitance is less than 95).
此外,實施例6~10(平均粒徑:10μm、DBP吸油量:180ml/100g、添加量:0.5~5.0質量%之石墨)中,可知使初始電容維持或提升,同時循環特性提升。其中,實施例6~9(平均粒徑:10μm、DBP吸油量:180ml/100g、添加量:0.5~3.0質量%之石墨)中,可知不僅循環特性提升,初始電容亦提升。又,實施例7~9(平均粒徑:10μm、DBP吸油量:180ml/100g、添加量:1.0~3.0質量%之石墨)中,可知初始電容提升的同時循環特性顯著提升(循環特性為130以上)。另,比較例4(未添加石墨之情形)中循環特性幾乎無變化,比較例5(石墨添加量為7質量%之情形)中初始電容、循環特性均降 低了。 Further, in Examples 6 to 10 (average particle diameter: 10 μm, DBP oil absorption: 180 ml/100 g, and addition amount: 0.5 to 5.0% by mass of graphite), it was found that the initial capacitance was maintained or increased, and the cycle characteristics were improved. Among them, in Examples 6 to 9 (average particle diameter: 10 μm, DBP oil absorption: 180 ml/100 g, and addition amount: 0.5 to 3.0% by mass of graphite), it was found that not only the cycle characteristics were improved but also the initial capacitance was also improved. Further, in Examples 7 to 9 (average particle diameter: 10 μm, DBP oil absorption: 180 ml/100 g, addition amount: 1.0 to 3.0% by mass of graphite), it was found that the cycle characteristics were remarkably improved while the initial capacitance was increased (the cycle characteristic was 130). the above). In addition, in the case of Comparative Example 4 (in the case where graphite was not added), there was almost no change in the cycle characteristics, and in the case of Comparative Example 5 (in the case where the amount of addition of graphite was 7 mass%), the initial capacitance and the cycle characteristics were all lowered. It is low.
又,實施例11~15(乙炔碳黑添加量:0.1~5.0質量%)中,可知即使在石墨(平均粒徑:10μm、DBP吸油量:180ml/100g)的添加量為1質量%這樣相對較少的情形下,初始電容仍然維持不變或提升,同時循環特性提升。其中,實施例11~14(乙炔碳黑添加量為0.1~3.0質量%)中,可知不僅循環特性提升,初始電容亦提升。又,實施例13及14(乙炔碳黑添加量為1.5~3.0質量%)中,可知初始電容提升的同時循環特性顯著提升(任一者之循環特性均為130以上)。另,比較例6(未添加乙炔碳黑之情形)中循環特性降低,比較例7(乙炔碳黑添加量為7質量%之情形)中初始電容、循環特性均降低了。 In addition, in Examples 11 to 15 (the amount of acetylene black added: 0.1 to 5.0% by mass), it is understood that the amount of addition of graphite (average particle diameter: 10 μm, DBP oil absorption: 180 ml/100 g) is 1% by mass. In less cases, the initial capacitance remains the same or increases, while the cycle characteristics increase. Among them, in Examples 11 to 14 (the amount of acetylene black added was 0.1 to 3.0% by mass), it was found that not only the cycle characteristics were improved but also the initial capacitance was also improved. Further, in Examples 13 and 14 (the amount of acetylene black added was 1.5 to 3.0% by mass), it was found that the cycle characteristics were remarkably improved while the initial capacitance was increased (any of the cycle characteristics were 130 or more). Further, in Comparative Example 6 (in the case where acetylene black was not added), the cycle characteristics were lowered, and in Comparative Example 7 (when the amount of acetylene black added was 7% by mass), the initial capacitance and cycle characteristics were all lowered.
另,實施例16(使用爐黑取代乙炔碳黑之情形)可知亦維持初始電容,且循環特性提升。然而,將實施例2與實施例16對比,可知相對於爐黑而言使用乙炔碳黑的情形下,不僅循環特性提升,初始電容亦提升。 Further, in Example 16 (in the case where furnace black was used instead of acetylene black), it was found that the initial capacitance was also maintained and the cycle characteristics were improved. However, comparing Example 2 with Example 16, it is understood that in the case where acetylene black is used for the furnace black, not only the cycle characteristics are improved, but also the initial capacitance is improved.
像這樣,藉由具備滿足本發明條件之負極板,便能獲得維持或提升初始電容且循環特性優良之控制閥式鉛蓄電池。 As described above, by providing the negative electrode plate satisfying the conditions of the present invention, it is possible to obtain a control valve type lead storage battery which maintains or raises the initial capacitance and has excellent cycle characteristics.
以上已具體說明了本發明之實施形態,但本發明並非限定於該些實施形態及實施例。也就是說,上述實施形態及實施例所記載條件,除非另有記載,否則可依據本發明之技術性思想而變更。 The embodiments of the present invention have been specifically described above, but the present invention is not limited to the embodiments and examples. In other words, the conditions described in the above embodiments and examples can be changed in accordance with the technical idea of the present invention unless otherwise stated.
按照本發明,針對在部分充電狀態下運用之控制閥式鉛蓄電池,使負極活性物質中除碳黑以外還含有平均粒徑90μm以下,且DBP吸油量55ml/100g以上之石墨,藉此便能提供一種循環特性優良之控制閥式鉛蓄電池。 According to the present invention, the control valve type lead storage battery used in the partially charged state can contain graphite having an average particle diameter of 90 μm or less and DBP oil absorption of 55 ml/100 g or more in addition to carbon black in the negative electrode active material. A control valve type lead storage battery excellent in cycle characteristics is provided.
Claims (8)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2013256387 | 2013-12-11 | ||
| JP2014068055 | 2014-03-28 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201535847A TW201535847A (en) | 2015-09-16 |
| TWI545831B true TWI545831B (en) | 2016-08-11 |
Family
ID=53371057
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW103143054A TWI545831B (en) | 2013-12-11 | 2014-12-10 | Control valve type leaded battery |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JP6112225B2 (en) |
| TW (1) | TWI545831B (en) |
| WO (1) | WO2015087749A1 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE112018002253T5 (en) | 2017-04-28 | 2020-01-23 | Gs Yuasa International Ltd. | LEAD ACID BATTERY |
| WO2019087680A1 (en) | 2017-10-31 | 2019-05-09 | 株式会社Gsユアサ | Lead storage battery |
| CN111106315A (en) * | 2019-12-05 | 2020-05-05 | 安徽理士电源技术有限公司 | Lead-acid storage battery with high charge acceptance by adopting carbon material |
| WO2021131033A1 (en) * | 2019-12-27 | 2021-07-01 | 昭和電工マテリアルズ株式会社 | Negative electrode material for lead acid storage batteries for system power stabilization or load leveling, and method for producing same |
| JP7348089B2 (en) * | 2020-01-23 | 2023-09-20 | 古河電池株式会社 | liquid lead acid battery |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05174825A (en) * | 1991-12-25 | 1993-07-13 | Shin Kobe Electric Mach Co Ltd | Lead battery |
| JP2002231247A (en) * | 2001-01-30 | 2002-08-16 | Shin Kobe Electric Mach Co Ltd | Control valve type lead storage battery |
| JP2007173112A (en) * | 2005-12-22 | 2007-07-05 | Ntt Data Ex Techno Corp | Anode active material for secondary battery, secondary battery and their manufacturing method |
| JP4523580B2 (en) * | 2006-12-19 | 2010-08-11 | エヌ・ティ・ティ・データ先端技術株式会社 | Negative electrode active material for secondary battery and intermediate kneaded material for producing them |
-
2014
- 2014-12-03 WO PCT/JP2014/081945 patent/WO2015087749A1/en not_active Ceased
- 2014-12-03 JP JP2015552400A patent/JP6112225B2/en active Active
- 2014-12-10 TW TW103143054A patent/TWI545831B/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| JPWO2015087749A1 (en) | 2017-03-16 |
| JP6112225B2 (en) | 2017-04-12 |
| WO2015087749A1 (en) | 2015-06-18 |
| TW201535847A (en) | 2015-09-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5857962B2 (en) | Lead acid battery | |
| US20130099749A1 (en) | Lead-acid battery | |
| MX2010009700A (en) | Lithium-sulfur battery and cathode therefore. | |
| TWI545831B (en) | Control valve type leaded battery | |
| US20140120386A1 (en) | Over-Saturated Absorbed Glass Mat Valve Regulated Lead-Acid Battery Comprising Carbon Additives | |
| JP5748091B2 (en) | Lead acid battery | |
| CN104769756A (en) | Compositions for enhancing deep-cycle performance of valve-regulated lead-acid batteries filled with gel electrolytes | |
| CN114242945B (en) | Method for determining ratio of negative electrode capacity to positive electrode capacity and related lithium ion battery | |
| JP2009048800A (en) | Manufacturing method of paste type positive electrode plate | |
| US20140050986A1 (en) | Active materials for lead acid battery | |
| WO2016178219A1 (en) | Lead acid battery with prolonged service life | |
| CN110690417A (en) | Positive electrode active material, positive electrode for lithium ion secondary battery, lithium ion secondary battery, and method for producing positive electrode active material | |
| JP5656116B2 (en) | Lead acid battery | |
| JP5545975B2 (en) | Positive electrode active material for lead storage battery and positive electrode plate for lead storage battery comprising the same | |
| JP6628070B2 (en) | Manufacturing method of positive electrode plate for control valve type lead-acid battery | |
| JP2002141066A (en) | Control valve type lead storage battery | |
| JP2011070870A (en) | Lead-acid battery | |
| JP2004327299A (en) | Sealed lead-acid storage battery | |
| JP6996274B2 (en) | Lead-acid battery | |
| JP5598368B2 (en) | Lead acid battery and negative electrode active material thereof | |
| JP4984430B2 (en) | Method for producing paste active material for negative electrode | |
| JP2004055309A (en) | Method for producing paste-like active material for positive electrode and lead storage battery using the same | |
| JP6164502B2 (en) | Lead acid battery | |
| JP6447866B2 (en) | Control valve type lead storage battery manufacturing method | |
| JP6304452B2 (en) | Negative electrode for lead-acid battery and lead-acid battery |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Annulment or lapse of patent due to non-payment of fees |