JP6825270B2 - Manufacturing method of positive electrode plate for lead-acid battery - Google Patents

Manufacturing method of positive electrode plate for lead-acid battery Download PDF

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JP6825270B2
JP6825270B2 JP2016174903A JP2016174903A JP6825270B2 JP 6825270 B2 JP6825270 B2 JP 6825270B2 JP 2016174903 A JP2016174903 A JP 2016174903A JP 2016174903 A JP2016174903 A JP 2016174903A JP 6825270 B2 JP6825270 B2 JP 6825270B2
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和磨 河上
和磨 河上
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Showa Denko Materials Co Ltd
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Hitachi Chemical Co Ltd
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Description

本発明は、鉛蓄電池用正極板の製造方法に関する。 The present invention relates to a method for manufacturing a positive electrode plate for a lead storage battery.

一般に、鉛蓄電池用正極板は次のように製造される。まず、酸化鉛を主成分とする鉛粉と、希硫酸と、水と、カットファイバー等の種々の添加物とを練合してペースト状活物質を作製した後、鉛又は鉛合金からなる集電体に該ペースト状活物質を充填して未乾燥極板を作製する。次に、多数の未乾燥極板を枠に懸垂積載し、高温高湿度の雰囲気中に所定の時間(例えば20時間以上)置き、熟成を行う(熟成工程)。その後、乾燥処理を行い、未化成の鉛蓄電池用正極板を製造する。 Generally, a positive electrode plate for a lead storage battery is manufactured as follows. First, a paste-like active material is prepared by kneading lead powder containing lead oxide as a main component, dilute sulfuric acid, water, and various additives such as cut fiber, and then a collection of lead or a lead alloy. The electric body is filled with the paste-like active material to prepare an undried electrode plate. Next, a large number of undried plates are suspended and loaded on a frame and placed in a high-temperature and high-humidity atmosphere for a predetermined time (for example, 20 hours or more) for aging (aging step). After that, a drying process is performed to manufacture a positive electrode plate for an unchemical lead-acid battery.

熟成工程においては、ペースト状活物質中の金属鉛を、水分を媒介させて酸化させることで酸化鉛、水酸化鉛、炭酸鉛等を生成させると共に、三塩基性硫酸鉛及び四塩基性硫酸鉛を成長させて活物質粒子間の結合力を高める。そして、集電体の表面の金属鉛を酸化させて酸化鉛、水酸化鉛、炭酸鉛等とし、該生成物と活物質中の生成物とを結合させて集電体と活物質との間の密着力も高める。このとき、四塩基性硫酸鉛の結晶成長を促進させると、乾燥に伴う活物質の収縮が低減できるため、集電体と活物質との間の密着性をより高めることができる。したがって、熟成が進行するに伴い、活物質中の金属鉛の量が減少して、熟成工程終了時には、一般には約6質量%以下となる。 In the aging step, metallic lead in the paste-like active material is oxidized by mediating water to generate lead oxide, lead hydroxide, lead carbonate, etc., and tribasic lead sulfate and tetrabasic lead sulfate. To increase the binding force between active material particles. Then, the metallic lead on the surface of the current collector is oxidized to lead oxide, lead hydroxide, lead carbonate, etc., and the product is combined with the product in the active material to be between the current collector and the active material. Also enhances the adhesion of. At this time, if the crystal growth of the tetrabasic lead sulfate is promoted, the shrinkage of the active material due to drying can be reduced, so that the adhesion between the current collector and the active material can be further enhanced. Therefore, as the aging progresses, the amount of metallic lead in the active material decreases, and at the end of the aging process, it is generally about 6% by mass or less.

一方、熟成することにより、正極活物質中の水分含有量も減少し、熟成工程終了時には、一般には4質量%以下となる。しかし、熟成工程における正極活物質中の水分含有量の急激な低下は、熟成乾燥後の正極板に剥離又は亀裂が生じる原因となり得る。このような問題に対し、例えば特許文献1には、熟成工程の途中で極板に水分を加えることにより、正極活物質中の水分含有量を増やす技術が開示されている。 On the other hand, by aging, the water content in the positive electrode active material also decreases, and at the end of the aging step, it is generally 4% by mass or less. However, a sharp decrease in the water content in the positive electrode active material in the aging step may cause peeling or cracking of the positive electrode plate after aging and drying. To solve such a problem, for example, Patent Document 1 discloses a technique for increasing the water content in the positive electrode active material by adding water to the electrode plate during the aging process.

特開平9−097604号公報Japanese Unexamined Patent Publication No. 9-097604

しかし、特許文献1に記載の技術では、断続的に水を加えているため、活物質中の水分含有量が上昇下降を繰り返しており、熟成中の集電体及び活物質における反応にばらつきが生じる場合がある。この場合、得られた正極板を用いた鉛蓄電池の寿命が低下するおそれがある。 However, in the technique described in Patent Document 1, since water is added intermittently, the water content in the active material repeatedly rises and falls, and the reaction in the current collector and the active material during aging varies. May occur. In this case, the life of the lead storage battery using the obtained positive electrode plate may be shortened.

そこで、本発明の目的は、鉛蓄電池の寿命を向上させることが可能な鉛蓄電池用正極板の製造方法を提供することにある。 Therefore, an object of the present invention is to provide a method for manufacturing a positive electrode plate for a lead storage battery, which can improve the life of the lead storage battery.

本発明は、正極活物質が充填された集電体を熟成する熟成工程を備える、鉛蓄電池用正極板の製造方法であって、熟成工程開始時の正極活物質中の水分含有量が8質量%以上であり、かつ、熟成工程において、12時間以上、正極活物質中の水分含有量を7質量%以上に維持する、鉛蓄電池用正極板の製造方法を提供する。 The present invention is a method for manufacturing a positive electrode plate for a lead storage battery, which comprises an aging step of aging a current collector filled with a positive electrode active material, wherein the water content in the positive electrode active material at the start of the aging process is 8 mass. % Or more, and in the aging step, a method for producing a positive electrode plate for a lead storage battery, which maintains the water content in the positive electrode active material at 7% by mass or more for 12 hours or more.

この製造方法では、熟成工程開始時の正極活物質中の水分含有量を8質量%以上とし、かつ、熟成工程において、正極活物質中の水分含有量が7質量%以上である状態を熟成開始から所定時間維持することによって、集電体及び活物質における反応を均一化することができ、また、正極活物質中の水分含有量が6〜7質量%近傍のときに生じる急速な金属鉛の酸化反応を熟成工程の後期に生じさせることができる。そのため、活物質及び集電体の金属鉛を十分に酸化鉛、水酸化鉛、炭酸鉛等に変換でき、また、四塩基性硫酸鉛の結晶成長を促進できる。したがって、活物質間及び集電体と活物質との間の結合を強固にでき、結果として、鉛蓄電池の寿命を向上させることが可能な正極板が得られる。 In this production method, the water content in the positive electrode active material at the start of the aging step is 8% by mass or more, and in the aging step, the water content in the positive electrode active material is 7% by mass or more. By maintaining for a predetermined time from the above, the reaction in the current collector and the active material can be homogenized, and the rapid metallic lead generated when the water content in the positive electrode active material is in the vicinity of 6 to 7% by mass. The oxidation reaction can occur later in the aging process. Therefore, the metallic lead of the active material and the current collector can be sufficiently converted into lead oxide, lead hydroxide, lead carbonate, etc., and the crystal growth of tetrabasic lead sulfate can be promoted. Therefore, a positive electrode plate capable of strengthening the bond between the active materials and between the current collector and the active material and, as a result, improving the life of the lead storage battery can be obtained.

この製造方法は、熟成工程前に、正極活物質が充填された集電体を、正極活物質中からの水分の蒸発を抑制する水分蒸発抑制手段で覆った状態で保管する工程を更に備えていてもよい。 This manufacturing method further includes a step of storing the current collector filled with the positive electrode active material in a state of being covered with a water evaporation suppressing means for suppressing the evaporation of water from the positive electrode active material before the aging process. You may.

この製造方法では、熟成工程において、正極活物質が充填された集電体を、正極活物質中からの水分の蒸発を抑制する水分蒸発抑制手段で覆った状態で熟成してもよい。 In this production method, in the aging step, the current collector filled with the positive electrode active material may be aged in a state of being covered with a water evaporation suppressing means for suppressing the evaporation of water from the positive electrode active material.

本発明によれば、鉛蓄電池の寿命を向上させることが可能な鉛蓄電池用正極板の製造方法を提供することができる。 According to the present invention, it is possible to provide a method for manufacturing a positive electrode plate for a lead storage battery, which can improve the life of the lead storage battery.

以下、本発明の実施形態について詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail.

鉛蓄電池用正極板(以下、単に「正極板」ともいう)の製造方法は、一態様において、集電体を作製する集電体作製工程と、正極活物質を作製する正極活物質作製工程と、集電体に正極活物質を充填する充填工程と、正極活物質が充填された集電体(未乾燥正極板ともいう)を熟成する熟成工程と、熟成後の未乾燥正極板を乾燥する乾燥工程とを備える。 In one embodiment, a method for manufacturing a positive electrode plate for a lead storage battery (hereinafter, also simply referred to as a “positive electrode plate”) includes a current collector manufacturing step for manufacturing a current collector and a positive electrode active material manufacturing step for manufacturing a positive electrode active material. , A filling step of filling the current collector with the positive electrode active material, a aging step of aging the current collector (also called an undried positive electrode plate) filled with the positive electrode active material, and drying the undried positive electrode plate after aging. It has a drying process.

集電体作製工程では、例えば格子状の集電体を作製する。集電体は、ブックモールド(重力鋳造)方式、連続鋳造方式、エキスパンド方式、打ち抜き方式等により鉛又は鉛合金を成形することで得られる。 In the current collector manufacturing step, for example, a grid-shaped current collector is manufactured. The current collector can be obtained by molding lead or a lead alloy by a book mold (gravity casting) method, a continuous casting method, an expanding method, a punching method, or the like.

正極活物質作製工程では、例えば、鉛粉、鉛丹、希硫酸、水及び添加剤を混合してペースト状正極活物質を得る。添加剤は、例えば活物質の強度を高める目的で添加され、PET(ポリエチレンテレフタレート)、アクリル系繊維等であってよい。 In the positive electrode active material manufacturing step, for example, lead powder, lead tan, dilute sulfuric acid, water and additives are mixed to obtain a paste-like positive electrode active material. The additive is added for the purpose of increasing the strength of the active material, and may be PET (polyethylene terephthalate), acrylic fiber, or the like.

充填工程では、例えば、上記のようにして得られた鉛又は鉛合金からなる格子状の集電体の格子間に、上記のようにして得られたペースト状正極活物質を充填する。これにより、正極活物質が充填された集電体(未乾燥正極板)が得られる。 In the filling step, for example, the paste-like positive electrode active material obtained as described above is filled between the lattices of the grid-like current collector made of lead or a lead alloy obtained as described above. As a result, a current collector (undried positive electrode plate) filled with the positive electrode active material can be obtained.

熟成工程では、未乾燥正極板を熟成する。熟成工程における温度は、例えば、60〜90℃、60〜70℃、70〜80℃、又は80〜90℃であってよい。熟成工程における相対湿度は、例えば、70〜100%、70〜80%、80〜90%、又は90〜100%であってよい。熟成工程における熟成時間は、例えば、20〜50時間、20〜30時間、30〜40時間、又は40〜50時間であってよい。 In the aging step, the undried positive electrode plate is aged. The temperature in the aging step may be, for example, 60 to 90 ° C, 60 to 70 ° C, 70 to 80 ° C, or 80 to 90 ° C. The relative humidity in the aging step may be, for example, 70-100%, 70-80%, 80-90%, or 90-100%. The aging time in the aging step may be, for example, 20 to 50 hours, 20 to 30 hours, 30 to 40 hours, or 40 to 50 hours.

熟成工程は、上記の条件で熟成を行う第1の工程と、第1の工程とは異なる条件で熟成を行う第2の工程とを備えていてもよい。 The aging step may include a first step of aging under the above conditions and a second step of aging under conditions different from the first step.

熟成工程では、熟成開始時の正極活物質中の水分含有量を8質量%以上とする。熟成開始時の正極活物質中の水分含有量は、鉛蓄電池の寿命を更に向上させる観点から、好ましくは9.0質量%以上、より好ましくは9.3質量%以上、更に好ましくは9.4質量%以上である。熟成開始時の正極活物質中の水分含有量は、例えば15質量%以下であってよい。正極活物質中の水分含有量は、例えば赤外線水分計(例えば株式会社ケット化学研究所製の製品名FD−720)を用いて測定される。 In the aging step, the water content in the positive electrode active material at the start of aging is set to 8% by mass or more. The water content in the positive electrode active material at the start of aging is preferably 9.0% by mass or more, more preferably 9.3% by mass or more, still more preferably 9.4, from the viewpoint of further improving the life of the lead storage battery. It is mass% or more. The water content in the positive electrode active material at the start of aging may be, for example, 15% by mass or less. The water content in the positive electrode active material is measured using, for example, an infrared moisture meter (for example, product name FD-720 manufactured by Kett Chemical Laboratory Co., Ltd.).

熟成工程では、熟成開始から12時間以上、正極活物質中の水分含有量を7質量%以上に維持する。正極活物質中の水分含有量を7質量%以上に維持する時間は、鉛蓄電池の寿命を更に向上させる観点から、好ましくは13時間以上、より好ましくは14時間以上、更に好ましくは15時間以上、特に好ましくは16時間以上である。正極活物質中の水分含有量を7質量%以上に維持する時間は、例えば30時間以下であってよい。 In the aging step, the water content in the positive electrode active material is maintained at 7% by mass or more for 12 hours or more from the start of aging. The time for maintaining the water content in the positive electrode active material at 7% by mass or more is preferably 13 hours or more, more preferably 14 hours or more, still more preferably 15 hours or more, from the viewpoint of further improving the life of the lead storage battery. Especially preferably, it is 16 hours or more. The time for maintaining the water content in the positive electrode active material at 7% by mass or more may be, for example, 30 hours or less.

熟成工程の全部又は一部において、未乾燥正極板を水分蒸発抑制手段で覆った状態で熟成してもよい。この場合、正極活物質中の水分含有量を7質量%以上に維持しやすくなる。水分蒸発抑制手段は、正極活物質中からの水分の蒸発を抑制可能なものであれば特に制限されない。水分蒸発抑制手段は、例えば、ポリエステル、ナイロン、含フッ素化合物等の撥水性材料で形成されたシート又は布であってよい。これらのシート及び布は、例えば未乾燥正極板を収容可能な袋状に成形されていてもよい。 In all or part of the aging step, the undried positive electrode plate may be aged in a state of being covered with a moisture evaporation suppressing means. In this case, it becomes easy to maintain the water content in the positive electrode active material at 7% by mass or more. The water evaporation suppressing means is not particularly limited as long as it can suppress the evaporation of water from the positive electrode active material. The water evaporation suppressing means may be, for example, a sheet or cloth formed of a water-repellent material such as polyester, nylon, or a fluorine-containing compound. These sheets and cloths may be formed in a bag shape capable of accommodating, for example, an undried positive electrode plate.

熟成工程に続く乾燥工程では、熟成後の未乾燥正極板を乾燥する。乾燥は、例えば、温度55〜65℃の環境で92〜192時間行われる。これにより、(未化)正極板が得られる。 In the drying step following the aging step, the undried positive electrode plate after aging is dried. Drying is carried out, for example, in an environment at a temperature of 55 to 65 ° C. for 92 to 192 hours. As a result, a (unconverted) positive electrode plate is obtained.

正極板の製造方法は、一態様において、充填工程と熟成工程との間に、正極活物質が充填された集電体(未乾燥正極板)を水分蒸発抑制手段で覆った状態で保管する保管工程を更に備えていてもよい。保管工程で用いる水分蒸発抑制手段は、上述したのと同様である。保管工程で用いる水分蒸発抑制手段と、熟成工程で用いる水分蒸発抑制手段とは、互いに同じであっても異なっていてもよい。 In one aspect, the method for manufacturing a positive electrode plate is a storage in which a current collector (undried positive electrode plate) filled with a positive electrode active material is stored in a state of being covered with a moisture evaporation suppressing means between a filling step and an aging step. Further steps may be provided. The water evaporation suppressing means used in the storage step is the same as described above. The water evaporation suppressing means used in the storage step and the water evaporation suppressing means used in the aging step may be the same or different from each other.

保管工程における温度は、例えば、0〜45℃、0〜15℃、15〜30℃、又は30〜45℃であってよい。保管工程における相対湿度は、例えば、10〜100%、10〜40%、40〜70%、又は70〜100%であってよい。保管工程における保管時間は、例えば、0時間を超え6時間以下、0時間を超え2時間以下、2〜4時間、又は4〜6時間であってよい。 The temperature in the storage step may be, for example, 0 to 45 ° C, 0 to 15 ° C, 15 to 30 ° C, or 30 to 45 ° C. The relative humidity in the storage step may be, for example, 10-100%, 10-40%, 40-70%, or 70-100%. The storage time in the storage step may be, for example, more than 0 hours and 6 hours or less, more than 0 hours and 2 hours or less, 2 to 4 hours, or 4 to 6 hours.

以上のようにして得られる正極板は、鉛蓄電池の正極板として用いられる。鉛蓄電池は、例えば、複数の上記正極板と、複数の負極板と、複数のセパレータと、中空状の電槽と、電槽を密閉する蓋体とを備えている。正極板と負極板とは交互に配置されており、各正極板と負極板との間にはセパレータが設けられている。このように積層された正極板、負極板及びセパレータからなる極板群が、電槽内に収容されている。蓋体には、例えば、電槽内の圧力を制御する制御弁と、正極板を外部に接続する正極端子と、負極板を外部に接続する負極端子とが設けられている。 The positive electrode plate obtained as described above is used as a positive electrode plate for a lead storage battery. The lead-acid battery includes, for example, a plurality of the positive electrode plates, a plurality of negative electrode plates, a plurality of separators, a hollow electric tank, and a lid for sealing the electric tank. The positive electrode plate and the negative electrode plate are arranged alternately, and a separator is provided between each positive electrode plate and the negative electrode plate. A group of electrode plates composed of a positive electrode plate, a negative electrode plate, and a separator laminated in this way is housed in an electric tank. The lid is provided with, for example, a control valve for controlling the pressure in the battery case, a positive electrode terminal for connecting the positive electrode plate to the outside, and a negative electrode terminal for connecting the negative electrode plate to the outside.

この鉛蓄電池では、活物質間及び集電体と活物質との間が強固に結合された上述の正極板が用いられているため、優れた寿命(特にサイクル寿命)が得られる。本実施形態の鉛蓄電池の用途としては、例えば、主電源用途(サイクルユース(Cycle Use))、バックアップ電源用途(トリクルユース(Trickle Use))等が挙げられるが、特に主電源用途(サイクルユース(Cycle Use))が好適である。 In this lead-acid battery, since the above-mentioned positive electrode plate in which the active materials and the current collector and the active material are firmly bonded is used, an excellent life (particularly, a cycle life) can be obtained. Examples of the use of the lead-acid battery of the present embodiment include main power supply use (Cycle Use), backup power supply use (Trickle Use), and the like, and in particular, main power supply use (cycle use (cycle use)). Cycle Use)) is preferable.

以下、実施例に基づいて本発明を更に具体的に説明するが、本発明は以下の実施例に限定されるものではない。 Hereinafter, the present invention will be described in more detail based on Examples, but the present invention is not limited to the following Examples.

実施例1〜2及び比較例1〜2に共通して、鉛紛10質量部、希硫酸(比重1.260)1質量部、及び水1質量部の割合で混合したペーストに、カットファイバーを添加して練合することによりペースト状正極活物質を得た。鉛−カルシウム合金を用いて鋳造した単板(高さ144mm、幅145.mm、厚み3.75mm)の集電体に、正極板1枚あたりのペースト状正極活物質の量が258gとなるようにペースト状正極活物質を充填した。 Common to Examples 1 and 2 and Comparative Examples 1 and 2, cut fibers are added to a paste mixed at a ratio of 10 parts by mass of lead powder, 1 part by mass of dilute sulfuric acid (specific gravity 1.260), and 1 part by mass of water. A paste-like positive electrode active material was obtained by adding and kneading. The amount of paste-like positive electrode active material per positive electrode plate is 258 g in a current collector of a single plate (height 144 mm, width 145. mm, thickness 3.75 mm) cast using a lead-calcium alloy. Was filled with a paste-like positive electrode active material.

その後、実施例1では、熟成工程前の保管工程中及び熟成工程中に、ペースト状正極活物質が充填された集電体をポリエステルで形成された撥水性の布で覆って風防した。保管工程及び熟成工程の条件は以下のとおりである。
保管工程:温度25℃、相対湿度60%で1時間
熟成工程:温度80℃、相対湿度98%、及び、温度65℃、相対湿度70%で各21時間
以上の工程を経ることにより、鉛蓄電池用正極板を製造した。
Then, in Example 1, during the storage step before the aging step and during the aging step, the current collector filled with the paste-like positive electrode active material was covered with a water-repellent cloth made of polyester to protect it from the wind. The conditions of the storage process and the aging process are as follows.
Storage process: Temperature 25 ° C., relative humidity 60% for 1 hour Aging process: Temperature 80 ° C., relative humidity 98%, and temperature 65 ° C., relative humidity 70% for 21 hours or more each, lead-acid battery A positive electrode plate for use was manufactured.

実施例2では、熟成工程前の保管工程中のみペースト状正極活物質が充填された集電体をポリエステルで形成された撥水性の布で覆って風防した以外は、実施例1と同様にして鉛蓄電池用正極板を製造した。 In Example 2, the same as in Example 1 except that the current collector filled with the paste-like positive electrode active material was covered with a water-repellent cloth made of polyester to protect it from the wind only during the storage step before the aging step. A positive electrode plate for a lead storage battery was manufactured.

比較例1では、熟成工程前の保管工程中のみペースト状正極活物質が充填された集電体を風防テントで風防した以外は、実施例1と同様にして鉛蓄電池用正極板を製造した。 In Comparative Example 1, a positive electrode plate for a lead storage battery was manufactured in the same manner as in Example 1 except that the current collector filled with the paste-like positive electrode active material was windshielded with a windshield tent only during the storage process before the aging process.

比較例2では、保管工程及び熟成工程のいずれにおいても風防しなかったこと以外は、実施例1と同様にして鉛蓄電池用正極板を製造した。 In Comparative Example 2, a positive electrode plate for a lead storage battery was manufactured in the same manner as in Example 1 except that the windshield was not provided in either the storage step or the aging step.

各実施例及び比較例における熟成開始時の正極活物質中の水分含有量Wを、赤外線水分計(株式会社ケット化学研究所製、製品名FD−720)を用いて130℃下で10分間測定し、下記式より求めた。
W(質量%)=(M1−M2)/M1×100
式中、M1は測定前(熟成工程開始時)の正極活物質の質量を表し、M2は測定後(130℃下で10分間経過後)の正極活物質の質量を表す。
The water content W in the positive electrode active material at the start of aging in each Example and Comparative Example was measured at 130 ° C. for 10 minutes using an infrared moisture meter (manufactured by Kett Chemical Laboratory Co., Ltd., product name FD-720). Then, it was calculated from the following formula.
W (mass%) = (M1-M2) / M1 × 100
In the formula, M1 represents the mass of the positive electrode active material before the measurement (at the start of the aging process), and M2 represents the mass of the positive electrode active material after the measurement (after 10 minutes have passed at 130 ° C.).

また、熟成工程中、1時間おきに正極活物質をサンプリングし、上記と同様の方法により正極活物質中の水分含有量を測定した。熟成工程開始時の正極活物質中の水分含有量、及び熟成工程において正極活物質中の水分含有量が7質量%未満となるまでの時間を表1に示す。 Further, during the aging process, the positive electrode active material was sampled every hour, and the water content in the positive electrode active material was measured by the same method as described above. Table 1 shows the water content in the positive electrode active material at the start of the aging step and the time until the water content in the positive electrode active material becomes less than 7% by mass in the aging step.

また、得られた正極板(未化正極板)についてXRD測定を行い、三塩基性希硫酸鉛と四塩基性希硫酸鉛とのXRDピーク強度比(3BS/4BS)を算出した。結果を表1に示す。 Further, XRD measurement was performed on the obtained positive electrode plate (unmodified positive electrode plate), and the XRD peak intensity ratio (3BS / 4BS) of tribasic dilute lead sulfate and tetrabasic dilute lead sulfate was calculated. The results are shown in Table 1.

一方、以下の手順に従って、鉛蓄電池を作製した。
まず、鉛粉10質量部、希硫酸(比重1.260)1質量部、及び水0.47質量部の割合で混合したペーストに、希硫酸バリウム、バニレックスN、アセチレンブラック、及びカットファイバーを添加して練合することによりペースト状負極活物質を得た。次いで、鉛−カルシウム合金を用いて鋳造した単板(高さ146mm、幅147mm、厚み2.2mm)の集電体に、負極板1枚あたりペースト状負極活物質の量が175gとなるようにペースト状負極活物質を充填し、鉛蓄電池用負極板を製造した。
上述の実施例及び比較例の各正極板8枚、負極板9枚、リテーナを用いて極板群を作製し、極板群を6個直列に接続した。その後、水槽内設定温度40℃にて0.2CA充電と0.2CA放電を3回繰り返した後、0.12CA充電を行い合計67時間かけて電槽化成を実施し、12V系の密閉形鉛蓄電池を作製した。
On the other hand, a lead storage battery was produced according to the following procedure.
First, dilute barium sulfate, vanillex N, acetylene black, and cut fiber are added to a paste mixed at a ratio of 10 parts by mass of lead powder, 1 part by mass of dilute sulfuric acid (specific gravity 1.260), and 0.47 parts by mass of water. And kneaded to obtain a paste-like negative electrode active material. Next, the amount of the paste-like negative electrode active material per negative electrode plate was 175 g in the current collector of a single plate (height 146 mm, width 147 mm, thickness 2.2 mm) cast using a lead-calcium alloy. A negative electrode plate for a lead storage battery was manufactured by filling with a paste-like negative electrode active material.
A group of electrode plates was prepared using 8 positive electrode plates, 9 negative electrode plates, and a retainer of each of the above-mentioned Examples and Comparative Examples, and 6 electrode plates were connected in series. After that, 0.2CA charging and 0.2CA discharging were repeated three times at a set temperature of 40 ° C. in the water tank, and then 0.12CA charging was performed to carry out battery chemical conversion over a total of 67 hours, and a 12V type sealed lead was used. A storage battery was manufactured.

得られた鉛蓄電池について、サイクル試験を実施した。サイクル試験条件は、2CA放電と休止を5回繰り返し、その後0.15CA、0.10CA、0.05CA、0.04CAの順に充電電流値をステップさせ、対放電量の115〜120%容量比となるように充電を行うパターンとした。なお、放電時の蓄電池電圧が8.75V以下となった時点で、サイクル寿命と判定した。サイクル試験の結果を表1に示す。 A cycle test was carried out on the obtained lead-acid battery. The cycle test condition is that 2CA discharge and pause are repeated 5 times, and then the charge current value is stepped in the order of 0.15CA, 0.10CA, 0.05CA, 0.04CA to obtain a volume ratio of 115 to 120% of the discharge amount. The pattern was set so that the battery would be charged. When the storage battery voltage at the time of discharge became 8.75 V or less, the cycle life was determined. The results of the cycle test are shown in Table 1.

Figure 0006825270
Figure 0006825270

表1より、熟成工程開始時の正極活物質の水分含有量を8質量%以上とし、かつ、熟成工程中に、12時間以上、正極活物質中の水分含有量を7質量%以上に維持することで、未化正極板の三塩基性希硫酸鉛と四塩基性希硫酸鉛のXRDピーク強度比(3BS/4BS)が小さくなることが確認された。なお、XRDピーク強度比が小さいほど、四塩基性希硫酸鉛の結晶成長は促進され、正極活物質と集電体とが強固に結合しているといえる。そして、この場合、サイクル寿命特性に優れ、長寿命の鉛蓄電池が得られることが分かった。 From Table 1, the water content of the positive electrode active material at the start of the aging process is 8% by mass or more, and the water content in the positive electrode active material is maintained at 7% by mass or more for 12 hours or more during the aging process. As a result, it was confirmed that the XRD peak intensity ratio (3BS / 4BS) of the tribasal dilute lead sulfate and the tetrabasic dilute lead sulfate of the denified positive electrode plate was reduced. It can be said that the smaller the XRD peak intensity ratio, the more the crystal growth of tetrabasic dilute lead sulfate is promoted, and the positive electrode active material and the current collector are firmly bonded. In this case, it was found that a lead-acid battery having an excellent cycle life characteristic and a long life can be obtained.

Claims (2)

正極活物質が充填された集電体を熟成する熟成工程を備える、鉛蓄電池用正極板の製造方法であって、
前記熟成工程前に、前記正極活物質が充填された集電体を、前記正極活物質中からの水分の蒸発を抑制する水分蒸発抑制手段で覆った状態で保管する工程を更に備え
前記熟成工程において、熟成開始時の前記正極活物質中の水分含有量が8質量%以上であり、かつ、熟成開始から12時間以上、前記正極活物質中の水分含有量を7質量%以上に維持する、鉛蓄電池用正極板の製造方法。
A method for manufacturing a positive electrode plate for a lead storage battery, which comprises a aging step of aging a current collector filled with a positive electrode active material.
Prior to the aging step, a step of storing the current collector filled with the positive electrode active material in a state of being covered with a water evaporation suppressing means for suppressing the evaporation of water from the positive electrode active material is further provided .
In the aging step, the water content in the positive electrode active material at the start of aging is 8% by mass or more, and the water content in the positive electrode active material is 7% by mass or more for 12 hours or more from the start of aging. A method of manufacturing a positive electrode plate for a lead-acid battery to be maintained .
正極活物質が充填された集電体を熟成する熟成工程を備える、鉛蓄電池用正極板の製造方法であって、
前記熟成工程において、前記正極活物質が充填された集電体を、前記正極活物質中からの水分の蒸発を抑制する水分蒸発抑制手段で覆った状態で熟成し、熟成開始時の前記正極活物質中の水分含有量が8質量%以上であり、かつ、熟成開始から12時間以上、前記正極活物質中の水分含有量を7質量%以上に維持する、鉛蓄電池用正極板の製造方法。
A method for manufacturing a positive electrode plate for a lead storage battery, which comprises a aging step of aging a current collector filled with a positive electrode active material.
In the aging step, the current collector filled with the positive electrode active material is aged in a state of being covered with a water evaporation suppressing means for suppressing the evaporation of water from the positive electrode active material, and the positive electrode activity at the start of aging is performed. A method for producing a positive electrode plate for a lead storage battery , wherein the water content in the substance is 8% by mass or more, and the water content in the positive electrode active material is maintained at 7% by mass or more for 12 hours or more from the start of aging .
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