JP6203472B2 - Lead acid battery - Google Patents
Lead acid battery Download PDFInfo
- Publication number
- JP6203472B2 JP6203472B2 JP2011219316A JP2011219316A JP6203472B2 JP 6203472 B2 JP6203472 B2 JP 6203472B2 JP 2011219316 A JP2011219316 A JP 2011219316A JP 2011219316 A JP2011219316 A JP 2011219316A JP 6203472 B2 JP6203472 B2 JP 6203472B2
- Authority
- JP
- Japan
- Prior art keywords
- mol
- density
- lead
- ions
- electrolyte
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000002253 acid Substances 0.000 title claims description 7
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 claims description 35
- -1 aluminum ions Chemical class 0.000 claims description 35
- 229910001416 lithium ion Inorganic materials 0.000 claims description 35
- 229910052782 aluminium Inorganic materials 0.000 claims description 34
- 239000003792 electrolyte Substances 0.000 claims description 21
- 239000008151 electrolyte solution Substances 0.000 claims description 17
- PIJPYDMVFNTHIP-UHFFFAOYSA-L lead sulfate Chemical compound [PbH4+2].[O-]S([O-])(=O)=O PIJPYDMVFNTHIP-UHFFFAOYSA-L 0.000 description 16
- 238000009825 accumulation Methods 0.000 description 11
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 230000007423 decrease Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 4
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 description 4
- 238000000498 ball milling Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229910014474 Ca-Sn Inorganic materials 0.000 description 2
- TZCXTZWJZNENPQ-UHFFFAOYSA-L barium sulfate Chemical compound [Ba+2].[O-]S([O-])(=O)=O TZCXTZWJZNENPQ-UHFFFAOYSA-L 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- INHCSSUBVCNVSK-UHFFFAOYSA-L lithium sulfate Inorganic materials [Li+].[Li+].[O-]S([O-])(=O)=O INHCSSUBVCNVSK-UHFFFAOYSA-L 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000019635 sulfation Effects 0.000 description 1
- 238000005670 sulfation reaction Methods 0.000 description 1
- RBTVSNLYYIMMKS-UHFFFAOYSA-N tert-butyl 3-aminoazetidine-1-carboxylate;hydrochloride Chemical compound Cl.CC(C)(C)OC(=O)N1CC(N)C1 RBTVSNLYYIMMKS-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- 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
- Secondary Cells (AREA)
Description
この発明は鉛蓄電池に関する。 The present invention relates to a lead storage battery.
自動車の燃費の改善を目的に、蓄電池への充電を制御する充電制御機能、あるいは停止時にエンジンをストップするアイドリングストップ機能を備えている自動車が普及しつつある。このような自動車では、充電不足な状態で使用されるため、負極に硫酸鉛が蓄積するサルフェーションにより鉛蓄電池が短寿命になる傾向がある。これに対して発明者は、電解液の密度を例えば1.265g/cm3以下と低くし、かつ電解液に所定量のアルミニウムイオンとリチウムイオンとを含有させることにより、負極への硫酸鉛の蓄積を特に少なくでき、かつ低温HR性能を向上させることができることを見出した。なお低温HR性能は低温でエンジンを始動する際の蓄電池の性能を表し、例えば低温HR容量で評価できる。 For the purpose of improving the fuel efficiency of automobiles, automobiles equipped with a charge control function for controlling charging of a storage battery or an idling stop function for stopping an engine when stopped are becoming widespread. In such an automobile, since it is used in a state where charging is insufficient, lead storage batteries tend to have a short life due to sulfation in which lead sulfate accumulates on the negative electrode. On the other hand, the inventor reduced the density of the electrolytic solution to, for example, 1.265 g / cm 3 or less, and contained lead sulfate in the negative electrode by containing a predetermined amount of aluminum ions and lithium ions in the electrolytic solution. It has been found that the low temperature HR performance can be improved with a particularly small amount. The low temperature HR performance represents the performance of the storage battery when starting the engine at a low temperature, and can be evaluated by, for example, the low temperature HR capacity.
関連する先行技術を示すと、特許文献1(WO2007/36979)は、電解液にアルミニウムイオンとリチウムイオンとを含有させることにより、アイドリングストップ寿命と電池の容量(5時間率容量)とに優れた鉛蓄電池が得られることを開示している。しかしながら電解液の密度の影響は検討されておらず、負極がカーボンブラックを含み、アルミニウムイオンを含み密度が1.28g/cm3の電解液を備えた蓄電池に言及しているに留まる。 As for related prior art, Patent Document 1 (WO2007 / 36979) is superior in idling stop life and battery capacity (5-hour rate capacity) by containing aluminum ions and lithium ions in the electrolytic solution. It discloses that a lead-acid battery is obtained. However, the influence of the density of the electrolytic solution has not been studied, and only mentions a storage battery in which the negative electrode contains carbon black and contains an aluminum ion and has a density of 1.28 g / cm 3 .
この発明の基本的課題は、硫酸鉛の蓄積が少なく、かつ同じ電解液密度の鉛蓄電池を基準として低温HR性能を向上させた鉛蓄電池を提供することにある。 A basic object of the present invention is to provide a lead storage battery that has low accumulation of lead sulfate and improved low-temperature HR performance on the basis of a lead storage battery having the same electrolyte density .
この発明は、正極板と負極板との間にセパレータを介在させた極板群を電槽内に収容すると共に、前記電槽内に電解液を保持させた鉛蓄電池において、前記電解液は20℃の満充電状態における密度が1.265g/cm 3 以下1.200g/cm 3 以上で、かつアルミニウムイオンを0.02mol/L以上で0.2mol/L以下、リチウムイオンを0.02mol/L以上で0.2mol/L以下含有することを特徴とする。 The present invention relates to a lead-acid battery in which an electrode plate group in which a separator is interposed between a positive electrode plate and a negative electrode plate is accommodated in a battery case, and the electrolyte solution is held in the battery case. The density in the fully charged state at ℃ is 1.265 g / cm 3 or less 1.200 g / cm 3 or more , aluminum ions 0.02 mol / L or more and 0.2 mol / L or less, lithium ions 0.02 mol / L or more and 0.2 mol / L L or less is contained.
最も好ましくは20℃の満充電状態における密度が1.260g/cm3以下で1.230g/cm3以上である。満充電状態とは充電率が実質的に100%である状態をいい、例えば10時間率電流等で、定格容量の150%程度充電すると満充電状態にできる。鉛蓄電池の種類は実施例の液式鉛蓄電池の他に制御弁式鉛蓄電池でも良い。以下、電解液の密度は20℃の満充電状態における密度を表すものとする。
Most preferably, the density in a fully charged state at 20 ° C. is 1.260 g / cm 3 or less and 1.230 g / cm 3 or more. The fully charged state refers to a state in which the charging rate is substantially 100%. For example, a full charged state can be obtained by charging about 150% of the rated capacity with a 10 hour rate current. The type of the lead storage battery may be a control valve type lead storage battery in addition to the liquid lead storage battery of the embodiment. Hereinafter, the density of the electrolytic solution represents the density in a fully charged state at 20 ° C.
鉛蓄電池の電解液へのアルミニウムイオンとリチウムイオンの効果は、電解液の密度を1.265g/cm3を境に変化する。即ち、アルミニウムイオンもリチウムイオンも含有しない電解液と、アルミニウムイオンとリチウムイオンとを含有する電解液との差は、電解液の密度が1.265g/cm3以下で特に大きくなる。そして電解液の密度が1.265g/cm3以下では、アルミニウムイオンとリチウムイオンとを含有させることにより、硫酸鉛の蓄積が特に少なくなる。このためアイドリングストップ寿命性能をさらに向上させることができる。 The effect of aluminum ions and lithium ions on the electrolyte of lead-acid batteries changes at the electrolyte density of 1.265 g / cm 3 . That is, the difference between the electrolytic solution containing neither aluminum ions nor lithium ions and the electrolytic solution containing aluminum ions and lithium ions is particularly large when the density of the electrolytic solution is 1.265 g / cm 3 or less. When the density of the electrolytic solution is 1.265 g / cm 3 or less, the accumulation of lead sulfate is particularly reduced by containing aluminum ions and lithium ions. For this reason, the idling stop life performance can be further improved.
電解液の密度を小さくすると、一般に大電流での放電性能が低下し、自動車用の鉛蓄電池の場合、低温HR性能の低下が問題になる。しかしながらアルミニウムイオンとリチウムイオンとを適正量含む電解液では、電解液の密度を小さくしているにもかかわらず、同じ密度の電解液でアルミニウムイオンもリチウムイオンも含まない場合を基準として、低温HR性能を向上させることができる。これは電解液の密度が小さい場合、アルミニウムイオンとリチウムイオンの組み合わせが低温HR性能を著しく向上させるためである。 When the density of the electrolytic solution is reduced, discharge performance at a large current generally decreases, and in the case of a lead storage battery for automobiles, a decrease in low-temperature HR performance becomes a problem. However, in an electrolyte containing appropriate amounts of aluminum ions and lithium ions , low-temperature HR is based on the case where the electrolyte has the same density but contains neither aluminum ions nor lithium ions , even though the density of the electrolyte is reduced. Performance can be improved. This is because when the density of the electrolytic solution is small, the combination of aluminum ions and lithium ions significantly improves the low temperature HR performance.
電解液の密度が1.265g/cm3以下での、アルミニウムイオンとリチウムイオンの効果を説明する。0.02mol/L以上で0.2mol/L以下のリチウムイオンを含む場合、アルミニウムイオンの効果は0.02mol/L以上の濃度で著しくなり、例えば0.01mol/Lの場合に比べ、0.02mol/Lでは硫酸鉛の蓄積量を著しく少なくできる。またアルミニウムイオンの濃度が0.2mol/Lを越えると、硫酸鉛の蓄積がむしろ多くなることがあり、低温HR性能も低下する。0.02mol/L以上で0.2mol/L以下のアルミニウムイオンを含む場合、リチウムイオン濃度を0.01mol/Lから0.02mol/Lに増すと、低温HR性能が著しく向上し、硫酸鉛の蓄積量も減少する。リチウムイオン濃度を0.2mol/L超としても、性能の向上は見られず、硫酸鉛の蓄積量が増すことがある。そしてリチウム資源は限られており、過剰使用は好ましくない。 The effect of aluminum ions and lithium ions when the electrolyte density is 1.265 g / cm 3 or less will be described. When lithium ions of 0.02 mol / L or more and 0.2 mol / L or less are contained, the effect of aluminum ions becomes significant at a concentration of 0.02 mol / L or more. Lead accumulation can be significantly reduced. Also, if the aluminum ion concentration exceeds 0.2 mol / L, lead sulfate accumulation may increase rather, and the low-temperature HR performance will also deteriorate. When aluminum ions of 0.02 mol / L or more and 0.2 mol / L or less are included, increasing the lithium ion concentration from 0.01 mol / L to 0.02 mol / L significantly improves the low-temperature HR performance and reduces the amount of lead sulfate accumulation To do. Even if the lithium ion concentration exceeds 0.2 mol / L, the performance is not improved and the amount of lead sulfate accumulation may increase. And lithium resources are limited, and overuse is not preferable.
電解液の密度が1.200g/cm3未満となると、低温HR性能が不足するようになるので、電解液の密度は1.200g/cm3以上が好ましく、特に1.230g/cm3以上が好ましい。アルミニウムイオンとリチウムイオンを含有しない場合を基準とする、アルミニウムイオンとリチウムイオンの組み合わせによる低温HR性能の向上は、密度が1.265g/cm3よりも1.250g/cm3でより大きくなるので、密度は1.260g/cm3以下で1.230g/cm3以上が最も好ましい。 If the density of the electrolyte is less than 1.200 g / cm 3, since such a shortage of low-temperature HR performance, the density of the electrolyte solution is preferably 1.200 g / cm 3 or more, particularly 1.230g / cm 3 or more. The improvement in low-temperature HR performance due to the combination of aluminum ions and lithium ions, based on the case of containing no aluminum ions and lithium ions, is greater at 1.250 g / cm 3 than at 1.265 g / cm 3. Is preferably 1.260 g / cm 3 or less and most preferably 1.230 g / cm 3 or more.
以下に、本願発明の最適実施例を示す。本願発明の実施に際しては、当業者の常識及び先行技術の開示に従い、実施例を適宜に変更できる。 Hereinafter, an optimum embodiment of the present invention will be described. In carrying out the present invention, the embodiments can be appropriately changed in accordance with common sense of those skilled in the art and disclosure of prior art.
ボールミル法で製造した鉛粉に合成樹脂繊維を加え、水と希硫酸とを加えてペースト化し、Pb-Ca-Sn系の正極格子に充填して熟成と乾燥とを施し、未化成の正極板とした。ボールミル法で製造した鉛粉に合成樹脂繊維と硫酸バリウムとカーボンブラックとリグニンとを加え、水と希硫酸とを加えてペースト化し、Pb-Ca-Sn系の負極格子に充填して熟成と乾燥とを施し、未化成の負極板とした。未化成の負極板を微孔質で袋状のポリエチレンセパレータで包み、未化成の負極板8枚と未化成の正極板7枚とを電槽に収容した。 Synthetic resin fibers are added to the lead powder produced by the ball mill method, and water and dilute sulfuric acid are added to make a paste. The Pb-Ca-Sn positive electrode lattice is filled with aging and drying, and the unformed positive electrode plate It was. Synthetic resin fibers, barium sulfate, carbon black and lignin are added to the lead powder produced by the ball mill method, and water and dilute sulfuric acid are added to form a paste, which is then filled into a Pb-Ca-Sn negative electrode lattice and aged and dried. To give an unformed negative electrode plate. The unformed negative electrode plate was wrapped with a microporous, bag-like polyethylene separator, and 8 unformed negative electrode plates and 7 unformed positive electrode plates were accommodated in a battery case.
アルミニウムイオン含有量とリチウムイオン含有量とが各々0〜0.3mol/Lとなるように硫酸アルミニウムと硫酸リチウムとを加え、かつ化成後の満充電の状態で20℃での密度が1.290〜1.200g/cm3となるように密度を変化させた希硫酸を調製した。この希硫酸を電槽に注ぎ、25℃の水槽内で電槽化成を行って、D23サイズの鉛蓄電池とした。正極格子及び負極格子の材質と製造方法は任意で、鉛粉はボールミル法によるものに限らず、バートン法等によるものでもよく、鉛丹等の含有量は任意である。また鉛粉への添加物の量と種類、不純物の含有量等は任意である。アルミニウムイオンとリチウムイオンを含有させるための化合物の種類は任意である。各試料は、電解液の密度とアルミニウムイオン含有量とリチウムイオン含有量の他は、全て同じ条件で製造した。 Aluminum sulfate and lithium sulfate are added so that the aluminum ion content and the lithium ion content are 0 to 0.3 mol / L, respectively, and the density at 20 ° C. is 1.290 to 1.200 g in a fully charged state after chemical conversion. Dilute sulfuric acid having a density changed so as to be / cm 3 was prepared. This dilute sulfuric acid was poured into a battery case, and a battery case was formed in a 25 ° C. water tank to obtain a D23 size lead-acid battery. The material and manufacturing method of the positive and negative grids are arbitrary, and the lead powder is not limited to the one based on the ball mill method, but may be one based on the Barton method or the like, and the content of the lead tan is arbitrary. Further, the amount and type of additives to the lead powder, the content of impurities, etc. are arbitrary. The kind of compound for containing aluminum ion and lithium ion is arbitrary. Each sample was manufactured under the same conditions except for the density of the electrolytic solution, the aluminum ion content, and the lithium ion content.
電解液の密度と組成が同じ蓄電池を3個ずつ用意し、低温HR放電試験(JIS D 5301:2006の9.5.3b)を行い、-15℃で300Aで放電した際に端子電圧が6Vに低下するまでの放電持続時間を測定した。低温HR放電試験の後に蓄電池を満充電し、50℃でアイドリングストップ寿命試験を行った。電池工業会規格では、アイドリングストップ寿命試験を、25℃で45A×59秒の放電と300A×1秒の放電と14Vで60秒の充電の充放電サイクルを繰り返し、3600サイクル毎に40〜48時間蓄電池を放置するとしている(SBA S 0101:2006)。ここでは周囲の気温を50℃に変更して試験した。これは低密度の電解液では高温で硫酸鉛の蓄積が進行しやすいことと、季節と地域によっては自動車のエンジンルーム内は50℃以上になることのためである。そしてアイドリングストップ寿命試験での充放電を25200サイクルで打ち切り、蓄電池を解体して負極の硫酸鉛蓄積量を測定した。 Prepare three storage batteries with the same density and composition of the electrolyte, conduct a low-temperature HR discharge test (9.5.3b of JIS D 5301: 2006), and the terminal voltage drops to 6V when discharged at -15 ° C and 300A. The discharge duration until it was measured was measured. After the low-temperature HR discharge test, the storage battery was fully charged and an idling stop life test was conducted at 50 ° C. According to the Battery Industry Association Standard, the idling stop life test was repeated at 45 ° C for 59 seconds at 25 ° C, 300 A for 1 second, and charged and discharged for 60 seconds at 14 V for 40 to 48 hours every 3600 cycles. The storage battery is left unattended (SBA S 0101: 2006). Here, the ambient temperature was changed to 50 ° C. for the test. This is because low-density electrolytes tend to accumulate lead sulfate at high temperatures and, depending on the season and region, the temperature in the engine compartment of an automobile can be over 50 ° C. Then, charging / discharging in the idling stop life test was stopped at 25200 cycles, the storage battery was disassembled, and the amount of lead sulfate accumulation in the negative electrode was measured.
3個の蓄電池の平均値で結果を表1に示し、アルミニウムイオン含有量を0.05mol/L、リチウムイオン含有量を0.1mol/Lに固定し、電解液の密度を変えた際の結果を図1に示す。また結果は、電解液の密度が同じで、アルミニウムイオンもリチウムイオンも含有しない比較例を100とする相対値で示す。なおアルミニウムイオン含有量とリチウムイオン含有量が共に0の場合、電解液の密度が低い程、硫酸鉛の蓄積量が減り、低温HR性能が低下する傾向にある。 The results are shown in Table 1 with the average values of the three storage batteries. The results are shown when the aluminum ion content is fixed at 0.05 mol / L and the lithium ion content is fixed at 0.1 mol / L, and the density of the electrolyte is changed. It is shown in 1. The results are shown as relative values with the comparative example having the same density of the electrolytic solution and containing neither aluminum ions nor lithium ions as 100. When both the aluminum ion content and the lithium ion content are 0, the lower the electrolyte density, the lower the amount of lead sulfate accumulated and the lower the low-temperature HR performance.
主な結果を図1に示す。アルミニウムイオンとリチウムイオンを共に含む電解液では、密度を1.280g/cm3から1.265g/cm3へ低下させると、硫酸鉛の蓄積が著しく少なくなり、電解液の密度をさらに低下させても、硫酸鉛の蓄積はほぼ同じである。低温HR容量では、密度が1.230g/cm3までは電解液の密度を小さくする程、アルミニウムイオンとリチウムイオンの効果が増して、これらのイオンを含有しない場合を基準とする低温HR性能が向上する。 The main results are shown in FIG. In electrolytes containing both aluminum ions and lithium ions, if the density is reduced from 1.280 g / cm 3 to 1.265 g / cm 3 , the accumulation of lead sulfate is significantly reduced, and even if the density of the electrolyte is further reduced, The accumulation of lead sulfate is almost the same. With low-temperature HR capacity, the effect of aluminum ions and lithium ions increases as the electrolyte density decreases until the density reaches 1.230 g / cm 3, improving low-temperature HR performance based on the case where these ions are not contained. To do.
電解液の密度を実施例での代表的な条件である1.265g/cm3に固定し、リチウムイオン濃度を0.1mol/Lに固定して、アルミニウムイオン濃度を変えると、0.01mol/Lと0.02mol/Lの間で、硫酸鉛の蓄積量が急変する。そして0.2mol/Lまではアルミニウムイオン濃度と共に硫酸鉛の蓄積量が減少するが、0.3mol/Lでは逆に増加する。低温HR容量はアルミニウムイオン濃度を0.2mol/Lから0.3mol/Lへ増加させると、大きく低下する。従ってアルミニウムイオン濃度を0.02mol/Lから0.2mol/Lとする。これらの点では、電解液の密度を1.230g/cm3に固定した場合も、同じ傾向を示す。 When the density of the electrolyte is fixed at 1.265 g / cm 3 , which is a typical condition in the examples, the lithium ion concentration is fixed at 0.1 mol / L, and the aluminum ion concentration is changed, 0.01 mol / L and 0.02 The amount of lead sulfate accumulation changes rapidly between mol / L. And the accumulated amount of lead sulfate decreases with aluminum ion concentration up to 0.2 mol / L, but conversely increases at 0.3 mol / L. The low-temperature HR capacity decreases greatly when the aluminum ion concentration is increased from 0.2 mol / L to 0.3 mol / L. Therefore, the aluminum ion concentration is set to 0.02 mol / L to 0.2 mol / L. In these respects, the same tendency is shown when the density of the electrolytic solution is fixed at 1.230 g / cm 3 .
電解液の密度を1.265g/cm3に固定し、アルミニウムイオン濃度を0.05mol/Lに固定して、リチウムイオン濃度を変えると、0.05mol/Lまではリチウムイオン濃度と共に硫酸鉛の蓄積量が減少するが、0.2mol/L以上では逆に増加する。低温HR容量はリチウムイオン濃度が0.05mol/Lで最大となり、それ以上リチウムイオン濃度を増しても向上しない。従ってリチウムイオン濃度を0.02mol/Lから0.2mol/Lとする。電解液の密度を1.230g/cm3に固定し、アルミニウムイオン濃度を0.05mol/Lに固定すると、0.2mol/Lまでリチウムイオン濃度と共に蓄電池の性能が向上する。このためリチウムイオン濃度を0.02mol/Lから0.2mol/Lとする。 The density of the electrolyte was fixed to 1.265 g / cm 3, to fix the aluminum ion concentration to 0.05 mol / L, when changing the lithium ion concentration, up to 0.05 mol / L is accumulation of lead sulfate with lithium ion concentration Although it decreases, it increases conversely at 0.2 mol / L or more. The low-temperature HR capacity reaches its maximum at a lithium ion concentration of 0.05 mol / L, and does not improve even if the lithium ion concentration is increased further. Therefore, the lithium ion concentration is changed from 0.02 mol / L to 0.2 mol / L. When the density of the electrolyte is fixed at 1.230 g / cm 3 and the aluminum ion concentration is fixed at 0.05 mol / L, the performance of the storage battery improves with the lithium ion concentration up to 0.2 mol / L. Therefore, the lithium ion concentration is set to 0.02 mol / L to 0.2 mol / L.
電解液の密度を1.250g/cm3あるいは1.200g/cm3とした蓄電池でも、リチウムイオン濃度が0.02mol/L以上で0.2mol/L以下、アルミニウムイオン濃度が0.02mol/L以上で0.2mol/L以下で、同様の結果が得られる。 Even in storage batteries with an electrolyte density of 1.250 g / cm 3 or 1.200 g / cm 3 , the lithium ion concentration is 0.02 mol / L or more and 0.2 mol / L or less, and the aluminum ion concentration is 0.02 mol / L or more and 0.2 mol / L. Below L, similar results are obtained.
Claims (1)
前記電解液は20℃の満充電状態における密度が1.265g/cm3以下1.200g/cm3以上で、かつアルミニウムイオンを0.02mol/L以上で0.2mol/L以下、リチウムイオンを0.02mol/L以上で0.2mol/L以下含有することを特徴とする、鉛蓄電池。 A lead-acid battery for an automobile having an idling stop function in which an electrode plate group in which a separator is interposed between a positive electrode plate and a negative electrode plate is accommodated in the battery case, and an electrolytic solution is held in the battery case. In
The electrolyte has a density of 1.265 g / cm 3 or less and 1.200 g / cm 3 or more in a fully charged state at 20 ° C., 0.02 mol / L to 0.2 mol / L of aluminum ions, and 0.02 mol / L of lithium ions. The lead acid battery characterized by containing 0.2 mol / L or less above.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011219316A JP6203472B2 (en) | 2011-10-03 | 2011-10-03 | Lead acid battery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2011219316A JP6203472B2 (en) | 2011-10-03 | 2011-10-03 | Lead acid battery |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2013080593A JP2013080593A (en) | 2013-05-02 |
| JP6203472B2 true JP6203472B2 (en) | 2017-09-27 |
Family
ID=48526828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2011219316A Active JP6203472B2 (en) | 2011-10-03 | 2011-10-03 | Lead acid battery |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP6203472B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6115841B2 (en) * | 2016-01-26 | 2017-04-19 | 株式会社Gsユアサ | Lead acid battery |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0679493B2 (en) * | 1986-07-11 | 1994-10-05 | 東海産業株式会社 | Lead-acid battery function recovery agent and lead-acid battery function recovery method |
| JP3584076B2 (en) * | 1995-02-23 | 2004-11-04 | 新日本石油株式会社 | Electrode composition |
| WO2007036979A1 (en) * | 2005-09-27 | 2007-04-05 | The Furukawa Battery Co., Ltd. | Lead storage battery and process for producing the same |
| JP2008243487A (en) * | 2007-03-26 | 2008-10-09 | Furukawa Battery Co Ltd:The | Lead acid battery |
-
2011
- 2011-10-03 JP JP2011219316A patent/JP6203472B2/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| JP2013080593A (en) | 2013-05-02 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP5618254B2 (en) | Lead acid battery | |
| JP5884528B2 (en) | Liquid lead-acid battery | |
| JP5769096B2 (en) | Lead acid battery | |
| JP5748091B2 (en) | Lead acid battery | |
| JP2015128053A (en) | Lead storage battery | |
| WO2015079668A1 (en) | Lead-acid battery | |
| JP2013084362A (en) | Lead battery | |
| JP2013134957A (en) | Method for manufacturing lead-acid battery, and lead-acid battery | |
| WO2013114822A1 (en) | Lead-acid battery | |
| CN104681879B (en) | Lead-acid battery | |
| JP6203472B2 (en) | Lead acid battery | |
| JP5637503B2 (en) | Lead acid battery | |
| JP6495862B2 (en) | Lead acid battery | |
| JP6589633B2 (en) | Lead acid battery | |
| JP5879888B2 (en) | Control valve type lead acid battery | |
| JP5708959B2 (en) | Lead acid battery | |
| JP5573785B2 (en) | Lead acid battery | |
| JP5578123B2 (en) | Liquid lead-acid battery | |
| JP2012138331A (en) | Lead storage battery and idling stop vehicle | |
| JP6115841B2 (en) | Lead acid battery | |
| WO2020066763A1 (en) | Lead battery | |
| JP2016119294A (en) | Lead-acid battery | |
| CN105720240B (en) | Lead-acid battery | |
| JP6649690B2 (en) | Lead storage battery | |
| JP2014137970A (en) | Lead-acid battery |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20140905 |
|
| A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20150424 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20150430 |
|
| A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20150615 |
|
| A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20160105 |
|
| A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20170609 |
|
| A521 | Written amendment |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20170609 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20170830 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 6203472 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |