JP2002097277A - Method of producing additive for lead storage battery and lead storage battery using the same - Google Patents

Method of producing additive for lead storage battery and lead storage battery using the same

Info

Publication number
JP2002097277A
JP2002097277A JP2000289690A JP2000289690A JP2002097277A JP 2002097277 A JP2002097277 A JP 2002097277A JP 2000289690 A JP2000289690 A JP 2000289690A JP 2000289690 A JP2000289690 A JP 2000289690A JP 2002097277 A JP2002097277 A JP 2002097277A
Authority
JP
Japan
Prior art keywords
lignin
lead
storage battery
lead storage
acid
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.)
Abandoned
Application number
JP2000289690A
Other languages
Japanese (ja)
Inventor
Takayuki Kimura
隆之 木村
Masayuki Terada
正幸 寺田
Koji Hayashi
晃司 林
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Resonac Corp
Original Assignee
Shin Kobe Electric Machinery Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shin Kobe Electric Machinery Co Ltd filed Critical Shin Kobe Electric Machinery Co Ltd
Priority to JP2000289690A priority Critical patent/JP2002097277A/en
Publication of JP2002097277A publication Critical patent/JP2002097277A/en
Abandoned legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Landscapes

  • Battery Electrode And Active Subsutance (AREA)
  • Phenolic Resins Or Amino Resins (AREA)
  • Secondary Cells (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a lead storage battery having a long life. SOLUTION: This additive for a lead storage battery is obtained by the steps of adding an acid to a lignocellulosic substance comprising a phenol derivative having a methoxy group, mixing and separating to obtain lignin, and polymerizing the lignin using formaldehyde. This lead storage battery uses the additive for the negative electrode.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、鉛蓄電池の長寿命
化に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to extending the life of a lead storage battery.

【0002】[0002]

【従来の技術】鉛蓄電池は、コスト及び信頼性の面で優
れていることから、無停電電源装置、自動車用バッテ
リ、電気自動車等の幅広い分野で使用されている。最
近、これらに用いられる鉛蓄電池の長寿命化が強く望ま
れている。
2. Description of the Related Art Lead-acid batteries are used in a wide range of fields such as uninterruptible power supplies, automobile batteries, and electric vehicles because of their excellent cost and reliability. Recently, it has been strongly desired to extend the life of lead-acid batteries used in these batteries.

【0003】鉛蓄電池を長寿命化するには、負極板に用
いられている活物質を微細化したり多孔質化したりする
ことによって、負極板の電極反応面積を大きくし、その
状態を長期間にわたって保持する必要がある。
To extend the life of a lead-acid battery, the active material used in the negative electrode plate is made finer or porous to increase the electrode reaction area of the negative electrode plate, and the state of the negative electrode plate is extended over a long period of time. Need to be retained.

【0004】なお、負極活物質を微細化したり多孔質化
する材料(以下、エキスパンダと呼ぶ)としてリグニン
があり、前記リグニンを負極活物質層に添加したり、負
極板と接触する部分のリテーナに含浸させる手法が有効
であることが知られている。
There is lignin as a material (hereinafter, referred to as an expander) for making the negative electrode active material finer or porous, and the lignin is added to the negative electrode active material layer or a retainer is provided at a portion in contact with the negative electrode plate. It is known that a technique of impregnating the sapphire is effective.

【0005】一方、上述したリグニンは、製紙工業にお
いてリグノセルロース(一般の木材等の草木類の構成物
質)からパルプ(セルロース)を生産する工程の副産物
として得ることができる。なお、前記リグニンは、木材
を形成している細胞と細胞の間に3次元の網目状に存在
しており、細胞間同士を繋ぐバインダーの働きをするも
のである。
[0005] On the other hand, the above-mentioned lignin can be obtained as a by-product of a process of producing pulp (cellulose) from lignocellulose (constituent substance of vegetation such as wood) in the papermaking industry. The lignin is present in a three-dimensional network between cells forming wood, and functions as a binder connecting the cells.

【0006】製紙工業では、木材を破砕したチップを、
アルカリ蒸解法(クラフト蒸解法とも呼ばれている)や
サルファイト蒸解法により、高温・高圧の条件下で蒸解
・処理して、セルロースとリグニンとに分離している。
[0006] In the paper industry, chips obtained by crushing wood are
It is separated into cellulose and lignin by digestion and treatment under conditions of high temperature and high pressure by alkaline cooking method (also called kraft cooking method) or sulfite cooking method.

【0007】なお、これらの手法で得られたリグニン
(以下、工業リグニンと呼ぶ)において、アルカリ蒸解
法で得られたリグニンをクラフトリグニンと呼び、サル
ファイト蒸解法で得られたリグニンをリグニンスルホン
酸と呼んでいる。
[0007] In the lignin obtained by these techniques (hereinafter referred to as industrial lignin), the lignin obtained by alkaline cooking is called kraft lignin, and the lignin obtained by sulfite cooking is called lignin sulfonic acid. I'm calling

【0008】[0008]

【発明が解決しようとする課題】しかしながら、上述し
た製紙工業における工業リグニンの製造は、高温・高圧
の条件下で行われるので、リグニンの3次元構造の一部
が破壊される。そして、得られた工業リグニンは、ラン
ダムにその構造が破壊されると共に、分子レベルにおい
ても高度に変性を受けており、それを構成している官能
基の不活性化が起こったり、その安定性が損なわれたり
している。
However, since the production of industrial lignin in the paper industry described above is performed under high temperature and high pressure conditions, a part of the three-dimensional structure of lignin is destroyed. The resulting industrial lignin has its structure destroyed randomly and is highly modified at the molecular level, resulting in inactivation of its constituent functional groups and its stability. Has been impaired.

【0009】これらの工業リグニンを、60°Cを超え
る高温環境下で使用される鉛蓄電池に使用した場合に
は、エキスパンダとしての効果が短期間に失われるとい
う問題点がある。
When these industrial lignins are used in lead storage batteries used in a high-temperature environment exceeding 60 ° C., there is a problem that the effect as an expander is lost in a short time.

【0010】なお、これらの工業リグニンに替わる添加
剤として、種々の有機化合物(スルホン酸系界面活性
剤、β−ナフタレンスルホン酸のホルマリン縮合物や高
分子系界面活性剤など)が検討されてきた。しかしなが
ら、上記した工業リグニンに替わるものが現在に至るま
で見いだされていないのが実状である。
Various organic compounds (sulfonic acid-based surfactants, formalin condensates of β-naphthalenesulfonic acid, polymer-based surfactants, etc.) have been studied as additives replacing these industrial lignins. . However, in reality, no substitute for the above-mentioned industrial lignin has been found up to the present.

【0011】本発明は上記した事案に鑑み、エキスパン
ダとしてより優れた効果を有するリグニンを用いること
によって、長寿命な鉛蓄電池を提供することを目的とし
ている。
The present invention has been made in consideration of the above circumstances, and has as its object to provide a long-life lead-acid battery by using lignin having a more excellent effect as an expander.

【0012】[0012]

【課題を解決するための手段】上記した課題を解決する
ために本発明では、フェノール誘導体が添加された木粉
に酸を加えてリグニンを抽出し、該リグニンを付加重合
させる方法で作製した添加剤を、鉛蓄電池用のエキスパ
ンダとして用いることを特徴としている。
In order to solve the above-mentioned problems, the present invention provides an additive prepared by a method in which lignin is extracted by adding an acid to wood powder to which a phenol derivative is added, and lignin is subjected to addition polymerization. The agent is used as an expander for a lead storage battery.

【0013】すなわち、第一の発明は、フェノール誘導
体が添加されたリグノセルロース系物質に酸を添加し、
混合・分離してリグニンを作成し、該リグニンを重合剤
を用いて重合させることを特徴とし、第二の発明は、前
記フェノール誘導体に、メトキシ基を有するものを用い
ることを特徴とし、第三の発明は、前記重合剤としてホ
ルムアルデヒドを使用することを特徴としている。
That is, the first invention is to add an acid to a lignocellulosic substance to which a phenol derivative is added,
A lignin is prepared by mixing and separating, and the lignin is polymerized using a polymerization agent.The second invention is characterized in that the phenol derivative has a methoxy group, and the phenol derivative has a methoxy group. The invention is characterized in that formaldehyde is used as the polymerization agent.

【0014】第四の発明は、前記した方法で作製した鉛
蓄電池用添加剤を鉛蓄電池の負極板中に用いることを特
徴とするするものである。
A fourth invention is characterized in that the additive for a lead storage battery produced by the above-mentioned method is used in a negative electrode plate of a lead storage battery.

【0015】[0015]

【発明の実施の形態】以下に、本発明の実施の形態につ
いて説明する。
Embodiments of the present invention will be described below.

【0016】1.リグニン1の作製 エキスパンダとしてのリグニン1は、以下の方法により
作製した。すなわち、リグノセルロースの粉末として、
広葉樹であるブナの木粉を使用した。なお、前記木粉の
平均粒子径は、約0.5mmである。
1. Preparation of Lignin 1 Lignin 1 as an expander was prepared by the following method. That is, as lignocellulose powder,
Beech wood flour, a hardwood, was used. The average particle diameter of the wood flour is about 0.5 mm.

【0017】フェノール誘導体として、2,6−ジメト
キシフェノールを用いた。前記2,6−ジメトキシフェ
ノール10gを、木粉が完全に浸る量のアセトンに溶解
させて溶液とした。これを前記木粉10gに加えて、ア
セトンが揮発しないように蓋をして24時間放置して木
粉の内部に十分に浸透させる。
As a phenol derivative, 2,6-dimethoxyphenol was used. 10 g of the 2,6-dimethoxyphenol was dissolved in an amount of acetone in which the wood flour was completely immersed to form a solution. This is added to 10 g of the wood flour, and the acetone is covered with a lid so as not to volatilize and left for 24 hours to sufficiently penetrate into the wood flour.

【0018】そして、大気中でアセトンを自然気化さ
せ、2,6−ジメトキシフェノールを含浸した木粉を得
た。
Then, acetone was spontaneously vaporized in the air to obtain wood powder impregnated with 2,6-dimethoxyphenol.

【0019】その後、前記2,6−ジメトキシフェノー
ルを含浸した木粉に、70質量%の硫酸50mlを加え
て、60分間室温で激しく攪拌する。ここに、フェノー
ル:ベンゼン=8:2(vol%)を50ml加える
と、木粉はセルロースを含んだ硫酸相とリグニンを含ん
だフェノール相に分離される。
Thereafter, 50 ml of 70% by weight sulfuric acid is added to the wood powder impregnated with 2,6-dimethoxyphenol, and the mixture is vigorously stirred at room temperature for 60 minutes. Here, when 50 ml of phenol: benzene = 8: 2 (vol%) is added, the wood flour is separated into a sulfuric acid phase containing cellulose and a phenol phase containing lignin.

【0020】この状態で遠心分離機を用いて、3500
rpm、10分間処理した後、リグニンを含むフェノー
ル相を大過剰のエチルエーテルに滴下させることで2,
6-ジメトキシフェノールが導入されたリグニンを抽出
した。以下、このリグニンをリグニン1と仮称する。
In this state, using a centrifuge, 3500
After treatment at 10 rpm for 10 minutes, the phenol phase containing lignin was added dropwise to a large excess of ethyl ether to give 2,2.
Lignin into which 6-dimethoxyphenol was introduced was extracted. Hereinafter, this lignin is temporarily referred to as lignin 1.

【0021】2.リグニン2の作製 エキスパンダとして、上記したリグニン1にホルムアル
デヒドによる付加縮合を行って分子量を増加させたリグ
ニン2を作製した。
2. Preparation of Lignin 2 As an expander, Lignin 2 having an increased molecular weight by subjecting the above lignin 1 to addition condensation with formaldehyde was prepared.

【0022】すなわち、前記リグニン1が32.0gと、
37質量%のホルムアルデヒド溶液を12.3gを混合し
た後、水酸化ナトリウム水溶液を加えながら混合し、溶
液中のアルカリ濃度を0.2Nとなるように調整する。
この溶液を70℃で2時間反応させた後、10質量%の
硫酸を加えて、溶液のpHを3〜4に調整する。この溶
液の沈殿区分であるリグニンを回収し、乾燥後、乳鉢で
粉砕して粉末としてリグニンを得た。以下、このリグニ
ンをリグニン2と仮称する。
That is, the lignin 1 is 32.0 g,
After mixing 12.3 g of a 37% by mass formaldehyde solution, the mixture is mixed while adding an aqueous sodium hydroxide solution to adjust the alkali concentration in the solution to 0.2N.
After the solution is reacted at 70 ° C. for 2 hours, 10% by mass of sulfuric acid is added to adjust the pH of the solution to 3-4. Lignin, which is a sedimentation section of this solution, was collected, dried, and ground in a mortar to obtain lignin as a powder. Hereinafter, this lignin is temporarily referred to as lignin 2.

【0023】3.リグニン3の作製 エキスパンダとして、上記したリグニン1に、前記した
リグニン2と異なる手法で、ホルムアルデヒドによる付
加縮合を行って分子量を増加させたリグニン3を作製し
た。
3. Preparation of Lignin 3 As an expander, lignin 3 was prepared by subjecting the above-mentioned lignin 1 to addition condensation with formaldehyde by a method different from that of the above-mentioned lignin 2 to increase the molecular weight.

【0024】すなわち、リグニン1が44.0gと、37
質量%のホルムアルデヒド溶液を9.2g、水1.3gを
混合し、10%硫酸を0.2g添加する。この酸性の溶
液を1.5時間、還流冷却器を用いて加熱還流する。こ
の溶液の沈殿区分であるリグニンを回収し、乾燥後、乳
鉢で粉砕して粉末としてリグニンを得た。以下、このリ
グニンをリグニン3と仮称する。
That is, 44.0 g of lignin 1 and 37
9.2 g of a mass% formaldehyde solution and 1.3 g of water are mixed, and 0.2 g of 10% sulfuric acid is added. The acidic solution is heated to reflux using a reflux condenser for 1.5 hours. Lignin, which is a sedimentation section of this solution, was collected, dried, and ground in a mortar to obtain lignin as a powder. Hereinafter, this lignin is temporarily referred to as lignin 3.

【0025】4.市販リグニン エキスパンダとして従来から使用している、市販のリグ
ニン粉末(商品名:INDULIN、Westvaco社製)を用い
た。このリグニン粉末は、木材を破砕したチップを、ア
ルカリ蒸解法によって生成したものである。
4. A commercially available lignin powder (trade name: INDULIN, manufactured by Westvaco), which has been conventionally used as a commercially available lignin expander, was used. This lignin powder is obtained by producing wood crushed chips by an alkaline cooking method.

【0026】上記したリグニン1〜3及び市販リグニン
は、溶媒としてTHF、カラムとしてKF804,KF
803,KF802,KF801を用いた高速液体クロマ
トグラフ(島津製作所製)で重量平均分子量を測定し
た。
The above-mentioned lignins 1 to 3 and commercially available lignin are THF as a solvent and KF804, KF as a column.
The weight average molecular weight was measured with a high performance liquid chromatograph (manufactured by Shimadzu Corporation) using 803, KF802, and KF801.

【0027】5.負極板 酸化鉛(PbO)を主成分とする鉛粉100質量部に、
硫酸バリウムを1質量部と、上述した各種のリグニンの
粉末を0.2質量部を添加・混合して混合物を作製す
る。そして、前記混合物中の鉛粉100質量部に対して
比重1.26の希硫酸10質量部と、水7質量部とを加
えて練合し、負極用のペースト状活物質を作製した。
5. Anode plate 100 parts by mass of lead powder mainly composed of lead oxide (PbO)
A mixture is prepared by adding and mixing 1 part by mass of barium sulfate and 0.2 part by mass of the various lignin powders described above. Then, 10 parts by mass of dilute sulfuric acid having a specific gravity of 1.26 and 7 parts by mass of water were added to 100 parts by mass of the lead powder in the mixture and kneaded to prepare a paste-like active material for a negative electrode.

【0028】このペースト状活物質を、l70mm×w
5mm×t2.4mmの鉛−カルシウム−錫合金からな
る集電体格子に充填して、温度45°C、湿度98RH
%の雰囲気下で24時間熟成させ、60°Cの雰囲気温
度で16時間乾燥させて未化板とした。この未化板を、
比重1.050の希硫酸中で24時間化成して負極板と
した。
[0028] The paste active material, l 70mm × w 4
Filled into a 5 mm × t 2.4 mm lead-calcium-tin alloy current collector grid, temperature 45 ° C., humidity 98 RH
%, And dried at an atmosphere temperature of 60 ° C. for 16 hours to obtain an unplated plate. This unplated plate,
A negative electrode plate was formed by chemical conversion in dilute sulfuric acid having a specific gravity of 1.050 for 24 hours.

【0029】6.正極板 正極板として、従来から使用しているものを用いた。す
なわち、酸化鉛(PbO)を主成分とする鉛粉100質
量部に対して比重1.34の希硫酸12質量部と、水1
5質量部とを加えて練合し、正極用のペースト状活物質
を作製した。
6. Positive Electrode Plate A conventionally used positive electrode plate was used. That is, 12 parts by mass of dilute sulfuric acid having a specific gravity of 1.34 and 100 parts by mass of lead powder containing lead oxide (PbO) as a main component,
5 parts by mass were added and kneaded to prepare a paste-like active material for a positive electrode.

【0030】このペースト状活物質を、l69mm×w
4mm×t3.7mmの鉛−カルシウム−錫合金からな
る集電体格子に充填して、温度45°C、湿度98RH
%の雰囲気下で24時間熟成させ、60°Cの雰囲気温
度で16時間乾燥させて未化板とした。この未化板を、
比重1.050の希硫酸中で24時間化成して正極板と
した。
The paste-like active material was obtained by adding 1 69 mm × w 4
4 mm × t 3.7 mm of lead - calcium - was filled in a collector Taikakuko consisting of tin alloy, the temperature 45 ° C, humidity 98RH
%, And dried at an atmosphere temperature of 60 ° C. for 16 hours to obtain an unplated plate. This unplated plate,
A positive electrode plate was formed by chemical conversion in dilute sulfuric acid having a specific gravity of 1.050 for 24 hours.

【0031】7.鉛蓄電池の製造・試験 上記した負極板4枚と正極板3枚とを、従来から使用し
ているリテーナを介して積層・溶接して極板群を組み立
て、該極板群をABS製の電槽に組込んで蓋をつけ、電
槽内に比重が1.31(20°C)の希硫酸電解液を5
6ml注液した後、密閉して7Ah−2Vの小形制御弁
式鉛蓄電池を作製した。
7. Manufacturing and Testing of Lead-Acid Batteries The above-mentioned four negative plates and three positive plates are laminated and welded via a conventionally used retainer to assemble an electrode group. Was assembled in an ABS battery case, and a lid was attached. A dilute sulfuric acid electrolyte solution having a specific gravity of 1.31 (20 ° C.) was placed in the battery case.
After injecting 6 ml, the container was sealed to produce a 7Ah-2V small-sized control valve type lead storage battery.

【0032】初期の小形制御弁式鉛蓄電池の放電容量
は、25℃中で、21A(3CA)の電流値で放電(放電
終止電圧:1.3V)して測定した。そして、制御弁式
鉛蓄電池の寿命は、加速試験法を用いた。すなわち、6
0℃の温度雰囲気中で2.275V/セルの定電圧で8
ヶ月の連続過充電を行い、定期的に25℃まで冷却した
後、21A(3CA)の電流値で放電して放電容量を測定
して、初期の放電容量と比較した。
The initial discharge capacity of the small control valve type lead-acid battery was measured at 25 ° C. by discharging at a current value of 21 A (3 CA) (discharge end voltage: 1.3 V). The life of the control valve type lead-acid battery was determined by using an accelerated test method. That is, 6
8 at a constant voltage of 2.275 V / cell in a temperature atmosphere of 0 ° C.
After performing continuous overcharge for a month and periodically cooling to 25 ° C., the battery was discharged at a current value of 21 A (3 CA), and the discharge capacity was measured and compared with the initial discharge capacity.

【0033】なお、前記した60℃、8ヶ月の連続過充
電試験後の放電容量は、一般的には25℃の環境下では
7年間使用した後の放電容量に相当するものと予想され
ている。
Incidentally, the discharge capacity after the above-mentioned continuous overcharge test at 60 ° C. for 8 months is generally expected to correspond to the discharge capacity after use for 7 years in an environment of 25 ° C. .

【0034】[0034]

【実施例】以下に本発明の実施例について説明する。Embodiments of the present invention will be described below.

【0035】(比較例1)酸化鉛(PbO)を主成分と
する鉛粉100重量部に、エキスパンダとして上記した
市販のリグニン粉末(商品名:INDULIN、Westvaco社
製)を0.2質量部添加して作製した負極板を用いた。
なお、この負極板の仕様は従来から使用していたもので
ある。その他の負極板や小形制御弁式鉛蓄電池の作製条
件及び小形制御弁式鉛蓄電池の試験条件は上記したもの
である。
Comparative Example 1 0.2 mass parts of the above-mentioned commercially available lignin powder (trade name: INDULIN, manufactured by Westvaco) as an expander was added to 100 parts by weight of lead powder mainly composed of lead oxide (PbO). A negative electrode plate prepared by addition was used.
The specifications of the negative electrode plate are those conventionally used. The other conditions for producing the negative electrode plate and the small control valve type lead-acid battery and the test conditions for the small control valve type lead-acid battery are as described above.

【0036】(比較例2)酸化鉛(PbO)を主成分と
する鉛粉100重量部に、エキスパンダとして上記した
リグニン1の粉末を0.2質量部添加して作製した負極
板を用いた。その他の負極板や小形制御弁式鉛蓄電池の
作製条件及び小形制御弁式鉛蓄電池の試験条件は上記し
たものである。
Comparative Example 2 A negative electrode plate prepared by adding 0.2 parts by weight of the above-mentioned lignin 1 powder as an expander to 100 parts by weight of lead powder containing lead oxide (PbO) as a main component was used. . The other conditions for producing the negative electrode plate and the small control valve type lead-acid battery and the test conditions for the small control valve type lead-acid battery are as described above.

【0037】(実施例1)酸化鉛(PbO)を主成分と
する鉛粉100重量部に、エキスパンダとして上記した
リグニン2の粉末を0.2質量部添加して作製した負極
板を用いた。その他の負極板や小形制御弁式鉛蓄電池の
作製条件及び小形制御弁式鉛蓄電池の試験条件は上記し
たものである。
Example 1 A negative electrode plate prepared by adding 0.2 parts by weight of the above-mentioned lignin 2 powder as an expander to 100 parts by weight of lead powder mainly containing lead oxide (PbO) was used. . The other conditions for producing the negative electrode plate and the small control valve type lead-acid battery and the test conditions for the small control valve type lead-acid battery are as described above.

【0038】(実施例2)酸化鉛(PbO)を主成分と
する鉛粉100重量部に、エキスパンダとして上記した
リグニン3の粉末を0.2質量部添加して作製した負極
板を用いた。その他の負極板や小形制御弁式鉛蓄電池の
作製条件及び小形制御弁式鉛蓄電池の試験条件は上記し
たものである。
(Example 2) A negative electrode plate prepared by adding 0.2 parts by mass of the above-mentioned lignin 3 powder as an expander to 100 parts by weight of lead powder containing lead oxide (PbO) as a main component was used. . The other conditions for producing the negative electrode plate and the small control valve type lead-acid battery and the test conditions for the small control valve type lead-acid battery are as described above.

【0039】表1に、各種エキスパンダの仕様、初期及
び60℃、8ヶ月後における小形制御弁式鉛蓄電池の放
電時間を示す。表1に示すように、本発明を用いた実施
例1〜2の電池は、比較例1、2の電池より長寿命であ
ることが分かる。そして、実施例1、2の結果に示すよ
うに、リグニン化合物の分子量が10000〜2000
0にするのが好ましいということがわかる。
Table 1 shows the specifications of the various expanders and the discharge time of the small control valve type lead-acid battery at the initial stage and at 60 ° C. for 8 months. As shown in Table 1, it can be seen that the batteries of Examples 1 and 2 using the present invention have a longer life than the batteries of Comparative Examples 1 and 2. Then, as shown in the results of Examples 1 and 2, the molecular weight of the lignin compound was 10,000 to 2,000.
It can be seen that it is preferable to set to 0.

【0040】従来のクラフト蒸解法やサルファイト蒸解
法によって得られたリグニンは、分子のランダム解重合
や自己縮合のために分子量がばらついており、且つ、エ
キスパンダとして有効に作用するフェノール基またはメ
トキシ基を失っているためと考えられる。
The lignin obtained by the conventional kraft digestion or sulfite digestion has a variable molecular weight due to random depolymerization or self-condensation of molecules, and has a phenol group or methoxy group which effectively acts as an expander. This is probably because the group has been lost.

【0041】一方、本発明を用いた場合には、その分子
量をほぼ一定にできるとともに、エキスパンダとして有
効に作用するフェノール基やメトキシ基が存在している
ため、小形制御弁式鉛蓄電池の長寿命化ができたものと
考えられる。
On the other hand, when the present invention is used, the molecular weight can be made substantially constant, and the presence of a phenol group or a methoxy group which effectively acts as an expander makes it possible to reduce the length of a small control valve type lead-acid battery. It is considered that the life was extended.

【0042】[0042]

【表1】 [Table 1]

【0043】上述した実施例では、小形制御弁式鉛蓄電
池に使用した場合について例示したが、本発明は鉛蓄電
池の用途や形状等に限定されることなく、上述した特許
請求の範囲において用いることができる。
In the above-described embodiment, the case where the present invention is applied to a small-sized control valve type lead-acid battery has been described. However, the present invention is not limited to the use and shape of the lead-acid battery, but may be used in the above-described claims. Can be.

【0044】なお、実施例ではフェノール誘導体とし
て、2,6−ジメトキシフェノールを用いたが、パラ−
クレゾール、カテコール、2−メトキシフェノール、
2,6−ジメチルフェノールなども用いることができ
る。
In the examples, 2,6-dimethoxyphenol was used as the phenol derivative.
Cresol, catechol, 2-methoxyphenol,
2,6-dimethylphenol and the like can also be used.

【0045】[0045]

【発明の効果】上述したように、本発明を用いることに
よって、鉛蓄電池の長寿命化が可能となり工業上優れた
ものである。
As described above, the use of the present invention makes it possible to extend the life of a lead storage battery, which is industrially excellent.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4J033 CA02 CA16 CA24 CA28 CA32 HB00 5H028 AA01 AA05 BB06 EE06 5H050 AA07 BA09 CA06 CB15 DA03 DA09 EA22 GA15  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 4J033 CA02 CA16 CA24 CA28 CA32 HB00 5H028 AA01 AA05 BB06 EE06 5H050 AA07 BA09 CA06 CB15 DA03 DA09 EA22 GA15

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】フェノール誘導体が添加されたリグノセル
ロース系物質に酸を添加し、混合・分離してリグニンを
作成し、該リグニンを重合剤を用いて重合させることを
特徴とする鉛蓄電池用添加剤の製造方法。
An additive for a lead storage battery, comprising adding an acid to a lignocellulosic substance to which a phenol derivative has been added, mixing and separating to form lignin, and polymerizing the lignin using a polymerizing agent. Method of manufacturing the agent.
【請求項2】前記フェノール誘導体として、メトキシ基
を有するものを用いることを特徴とする請求項1記載の
鉛蓄電池用添加剤の製造方法。
2. The method for producing an additive for a lead storage battery according to claim 1, wherein a phenol derivative having a methoxy group is used.
【請求項3】前記重合剤として、ホルムアルデヒドを使
用することを特徴とする請求項1又は2記載の鉛蓄電池
用添加剤の製造方法。
3. The method for producing an additive for a lead storage battery according to claim 1, wherein formaldehyde is used as said polymerizing agent.
【請求項4】請求項1〜3に記載の鉛蓄電池用添加剤
を、鉛蓄電池の負極板中に用いることを特徴とする鉛蓄
電池。
4. A lead-acid battery, wherein the additive for a lead-acid battery according to claim 1 is used in a negative electrode plate of the lead-acid battery.
JP2000289690A 2000-09-25 2000-09-25 Method of producing additive for lead storage battery and lead storage battery using the same Abandoned JP2002097277A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000289690A JP2002097277A (en) 2000-09-25 2000-09-25 Method of producing additive for lead storage battery and lead storage battery using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000289690A JP2002097277A (en) 2000-09-25 2000-09-25 Method of producing additive for lead storage battery and lead storage battery using the same

Publications (1)

Publication Number Publication Date
JP2002097277A true JP2002097277A (en) 2002-04-02

Family

ID=18773039

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2002097277A (en)

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