JPH0269523A - Treatment of polymer electrolyte - Google Patents

Treatment of polymer electrolyte

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Publication number
JPH0269523A
JPH0269523A JP22204688A JP22204688A JPH0269523A JP H0269523 A JPH0269523 A JP H0269523A JP 22204688 A JP22204688 A JP 22204688A JP 22204688 A JP22204688 A JP 22204688A JP H0269523 A JPH0269523 A JP H0269523A
Authority
JP
Japan
Prior art keywords
polymer electrolyte
carbon monoxide
polymer
olefin
ethylene
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.)
Pending
Application number
JP22204688A
Other languages
Japanese (ja)
Inventor
Yoshihisa Watanabe
渡辺 芳久
Makoto Takeda
武田 眞
Hisao Kinoshita
久夫 木下
Akiko Fujishima
藤島 明子
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.)
Mitsubishi Petrochemical Co Ltd
Original Assignee
Mitsubishi Petrochemical 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 Mitsubishi Petrochemical Co Ltd filed Critical Mitsubishi Petrochemical Co Ltd
Priority to JP22204688A priority Critical patent/JPH0269523A/en
Publication of JPH0269523A publication Critical patent/JPH0269523A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To readily decompose a polymer electrolyte into low-molecular substances and to eliminate environmental pollution by irradiating a copolymer consisting of an unsaturated carboxylic acid, olefin and carbon monoxide with light rays of specific wavelength. CONSTITUTION:A polymer obtained from an unsaturated carboxylic acid (e.g., maleic acid or acrylic acid), an olefin (e.g., ethylene or propylene) and carbon monoxide is irradiated with light rays (e.g., high-pressure mercury vapor lamp, xenon short arc lamp or sunlight) having 2,200-6,000Angstrom wavelength and treated.

Description

【発明の詳細な説明】 「産業上の利用分野」 本発明は新規な高分子電解質の処理方法に関するもので
ある。更に詳しくは高分子電解質を簡易に分解すること
により使用後環境への残留、蓄積等の問題のない新規な
高分子電解質の処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a novel method for treating a polymer electrolyte. More specifically, the present invention relates to a novel method for treating a polymer electrolyte that does not cause problems such as residual or accumulation in the environment after use by easily decomposing the polymer electrolyte.

無水マレイン酸、アクリル酸等の不飽和カルボン酸、オ
レフィン、一酸化炭素の共重合により得られる高分子電
解質は、分子中に多数のカルボキシル基および/または
その塩、ならびに主鎖中に多数のカルボニル基を有し、
吸水材料として多用されるほか各種の増粘剤、凝集剤、
洗剤用ビルダー等広い範囲で使用され極めて有用な高分
子材料である。
Polymer electrolytes obtained by copolymerizing unsaturated carboxylic acids such as maleic anhydride and acrylic acid, olefins, and carbon monoxide have many carboxyl groups and/or their salts in the molecule, and many carbonyl groups in the main chain. has a group,
In addition to being widely used as a water-absorbing material, it is also used as a variety of thickeners, flocculants,
It is an extremely useful polymeric material that is used in a wide range of applications, including detergent builders.

「従来の技術」 従来から、高分子電解質として、分子中に多数のカルボ
キシル基を有する多くの高分子化合物が知られており、
例えばポリアクリル酸、マレイン酸とオレフィンの共重
合物等が代表的なものであるが、これらの高分子化合物
は、分解性に乏しく使用後の残留物による環境汚染の発
生が懸念されるため、使用後排水として放出される洗剤
ビルグー等として使用する事は困難であった。
"Prior Art" Many polymer compounds having a large number of carboxyl groups in their molecules have been known as polymer electrolytes.
Typical examples include polyacrylic acid and copolymers of maleic acid and olefin, but these polymer compounds have poor degradability and there is concern that the residue after use may cause environmental pollution. It was difficult to use it as a detergent, such as bilgu, which is discharged as wastewater after use.

一方、本発明者らは、従来の高分子化合物に比し、分解
性に優れる新規な、オレフィンの共存下に一酸化炭素と
無水マレイン酸および/またはアクリル酸等の不飽和カ
ルボン酸とを共重合することにより得られる主鎖中にケ
トン基を含有する高分子化合物を見出した。
On the other hand, the present inventors have developed a new method that combines carbon monoxide and unsaturated carboxylic acids such as maleic anhydride and/or acrylic acid in the coexistence of an olefin, which has superior decomposition properties compared to conventional polymer compounds. We have discovered a polymer compound containing ketone groups in its main chain obtained by polymerization.

「発明が解決しようとする課題」 しかしながら、上記の主鎖中にCO基を含む新蜆な高分
子化合物であっても、その分解性は、使用後の廃棄物に
よる環境汚染の恐れのない、高吸水性樹脂、洗剤用ビル
ダー等の高分子電解質の応用、利用範囲を大きく拡大す
るには未だ十分とはいえないものである。特に我国では
洗剤用ビルダーとして燐を含有するトリポリ燐酸ソーダ
等の縮合燐酸塩は湖沼や河川の富栄養化を招くため事実
上使用が禁止されている。前記した主鎖中にCO基を含
む高分子化合物は優れた性能を有するトリポリ燐酸ソー
ダ等の縮合燐酸塩に匹敵するヒルダー性能を有しかつ湖
沼や河川の汚染を招くおそれのない新規なビルダーの提
供を可能とするものであり、その分解性を向上させる方
法が求められていた。
``Problem to be solved by the invention'' However, even with the above-mentioned new polymer compound containing CO groups in its main chain, its degradability is such that there is no risk of environmental pollution due to waste after use. It is still not enough to greatly expand the range of applications and uses of polymer electrolytes such as super absorbent resins and detergent builders. Particularly in Japan, the use of condensed phosphates such as sodium tripolyphosphate containing phosphorus as a builder for detergents is practically prohibited because it causes eutrophication of lakes and rivers. The above-mentioned polymeric compound containing a CO group in its main chain is a novel builder that has excellent Hilder performance comparable to condensed phosphates such as sodium tripolyphosphate and does not cause pollution of lakes and rivers. Therefore, there was a need for a method to improve the decomposability.

「課題を解決するための手段」 本発明者らは、それらの問題点の解決方法について種々
検討を重ねて来たがその結果、上記高分子化合物が波長
2200〜6000オングストロームの光により容易に
低分子化し、環境中で微生物により極めて容易に分解さ
れる事を見いだし本発明に到達した。
"Means for Solving the Problems" The present inventors have repeatedly studied various ways to solve these problems, and as a result, they have found that the above-mentioned polymer compounds are easily degraded by light with a wavelength of 2200 to 6000 angstroms. The present invention was achieved by discovering that it is molecularized and decomposed extremely easily by microorganisms in the environment.

「発明の構成」 本発明の対象とする共重合体は、エチレン、プロピレン
、ブテン類、スチレン、シクロペンテン、シクロヘキセ
ン、シクロオクテン、ビニルシクロヘキサン等各種の直
鎖、分枝、環状等の各種のオレフィンとマレイン酸、ア
クリル酸等の不飽和カルボン酸と一酸化炭素の三成分を
共重合することにより高分子の主鎖中にcodを有する
分子量5、000以上1,000.000以下の高分子
化合物である。
"Structure of the Invention" The copolymers of the present invention are copolymers with various linear, branched, and cyclic olefins such as ethylene, propylene, butenes, styrene, cyclopentene, cyclohexene, cyclooctene, and vinylcyclohexane. A polymer compound with a molecular weight of 5,000 to 1,000,000 that has COD in the main chain of the polymer is produced by copolymerizing three components: unsaturated carboxylic acids such as maleic acid and acrylic acid, and carbon monoxide. be.

この化合物は分子中にCO酸成分モル%で0.1〜20
%、好ましくは1〜15%含有している、これ以上CO
の含量が少な過ぎると充分な分解性が得られず、また高
過ぎても分解性が強過ぎて好ましくない、又、オレフィ
ン成分は5〜70%、好ましくは10〜60%、カルボ
ン酸成分をそれぞれ5〜80%、好ましくは20〜70
%含有する。
This compound has a CO acid component of 0.1 to 20 mol% in the molecule.
%, preferably 1-15%, no more CO
If the content of 5 to 80%, preferably 20 to 70% respectively
%contains.

この高分子化合物は、無水マレイン酸および/またはア
クリル酸(塩)、エチレン、プロピレン等のオレフィン
、一酸化炭素を触媒またはラジカル開始剤の存在下で重
合することにより比較的容易に製造することが可能であ
る。例えばラジカル重合に使用される熱、光、放射線等
による開始反応も可能であるが、通常良く行なわれるラ
ジカル開始剤の存在下で反応する方法が最も一般的であ
る。また、この反応を高収率で進行させるにはオレフィ
ンの共存が必須であり、それ以外反応条件には特別の限
定はないが、好ましくは一酸化炭素圧2〜800気圧、
オレフィン/一酸化炭素モル比0.01〜10、更に好
ましくは0.1〜5程度、反応温度は使用するラジカル
開始剤の分解条件に合わせ設定されるが、通常室温〜2
50℃程度の温度範囲が使用される。ラジカル開始剤と
しては通常使用される過酸化物、アゾビスニトリル類等
何でも使用可能であり、無機過酸化物、例えば過酸化水
素、過硫酸等、アゾビスニトリル類、アゾおよびジアゾ
化合物、有機過酸化物、その他芳香族スルフィン酸、l
−アルカンスルフィン酸およびそれらの塩等も使用され
る。
This polymer compound can be produced relatively easily by polymerizing maleic anhydride and/or acrylic acid (salt), olefins such as ethylene and propylene, and carbon monoxide in the presence of a catalyst or radical initiator. It is possible. For example, an initiation reaction using heat, light, radiation, etc. used in radical polymerization is also possible, but the most common method is to carry out the reaction in the presence of a radical initiator, which is commonly carried out. In addition, in order for this reaction to proceed in high yield, the coexistence of an olefin is essential, and other than that, there are no particular limitations on the reaction conditions, but preferably a carbon monoxide pressure of 2 to 800 atmospheres,
The olefin/carbon monoxide molar ratio is about 0.01 to 10, more preferably about 0.1 to 5.The reaction temperature is set according to the decomposition conditions of the radical initiator used, but is usually room temperature to 2.
A temperature range of around 50°C is used. As the radical initiator, any commonly used peroxide, azobisnitrile, etc. can be used, and inorganic peroxides such as hydrogen peroxide, persulfuric acid, azobisnitrile, azo and diazo compounds, organic peroxides, etc. oxides, other aromatic sulfinic acids, l
-Alkanesulfinic acids and their salts, etc. are also used.

反応の溶媒は、原料である無水マレイン酸の溶解性、ラ
ジカル開始剤の分解性等から任意に選定サレるが、ベン
ゼン、トルエン、エチルベンゼン、キシレン等の芳香族
化合物、クロロホルム、四塩化炭素等の有機ハロゲン化
物、アセトン、メチルエチルケトン等のケトン類、酢酸
メチル、酢酸エチル等のエステル類等が一般に使用され
る。
The reaction solvent can be selected arbitrarily based on the solubility of the raw material maleic anhydride, the decomposability of the radical initiator, etc., but aromatic compounds such as benzene, toluene, ethylbenzene, xylene, chloroform, carbon tetrachloride, etc. Organic halides, ketones such as acetone and methyl ethyl ketone, and esters such as methyl acetate and ethyl acetate are generally used.

共重合組成物の平均分子量は反応温度、原料濃度、圧力
、ラジカル開始剤の濃度、種類等の条件により変化する
ことが可能であり、用途によりs、ooo〜500.0
00の範囲に制御される。
The average molecular weight of the copolymer composition can vary depending on conditions such as reaction temperature, raw material concentration, pressure, concentration and type of radical initiator, and ranges from s, ooo to 500.0 depending on the use.
Controlled within the range of 00.

波長2200〜6000オングストロームを有する光を
照射する光源としては、高圧水銀ランプ、キセノンシッ
ートアークランプ、及び太陽光が挙げられる。
Examples of light sources that emit light having a wavelength of 2,200 to 6,000 angstroms include high-pressure mercury lamps, xenon seat-arc lamps, and sunlight.

照射時間は、光源及び共重合体中のCO基含有量により
異なるが、光照射後の分解物の分子量が2.500以下
、好ましくは2,000以下となるように適宜選定する
のが好ましい0例えば、100W高圧水銀ランプを用い
た場合、CO含110モル%のもので約8時間程度の照
射でも、重量平均分子量200.000程度のものが、
1000以下に低下する。光分解後のCO全含量数%か
らtraceであり、このものは、極めて容易に微生物
により分解される。
The irradiation time varies depending on the light source and the CO group content in the copolymer, but it is preferably selected appropriately so that the molecular weight of the decomposed product after light irradiation is 2.500 or less, preferably 2,000 or less. For example, when a 100W high-pressure mercury lamp is used, even when irradiated for about 8 hours with a 110 mol% CO containing lamp, a lamp with a weight average molecular weight of about 200,000
It decreases to 1000 or less. The total CO content after photolysis is traceable to several percent, and this is extremely easily decomposed by microorganisms.

「実施例」 以下に実施例をあげて本発明を具体的に説明するが、本
発明はこれらの実施例のみに限定されるものでないこと
は言うまでもない。
"Examples" The present invention will be specifically explained below with reference to Examples, but it goes without saying that the present invention is not limited only to these Examples.

尚実施例で行った試験方法は、該高分子電解質水溶液を
光分解装置を用い、分子量の変化をGPCで測定した。
In the test method carried out in the Examples, the polymer electrolyte aqueous solution was measured using a photolysis device, and the change in molecular weight was measured by GPC.

詳細を以下に示す。Details are shown below.

[光分解性試験条件] 100W 高圧水銀ランプ 温度=27℃ 高分子電解質1%水溶液:200m1 [分子量測定条件] GPC法 カラム: 5hodex 0Hpak 流速: 1 ml/min カラム温度:40°C 溶離液: 0.05M−KC7!水溶液[比較例] 誘導撹拌機及び、外部加熱ヒーターを、備えたハステロ
イ−C製オートクレーブに、無水マレイン酸30gr、
ベンゾイルペルオキシ)” 0.3 grを、含むベン
ゼン溶液100m1を仕込んだ。次いでオートクレーブ
を密封し、10kg/c++IC加圧エチレンで6回置
換した後、圧力計換算で50kg/cにGエチレンを導
入した。一定の撹拌を行いながら、加熱用ヒーターでオ
ートクレーブ中の反応混合物の温度を、70±2℃に調
節し4時間反応を行った。その後反応器を冷却し脱ガス
した後、開放してスラリーを取り出した。スラリーを2
00m1エーテル中に添加後、不溶性物質を濾別し、エ
ーテル洗浄後、乾燥処理を行い共重合物22.3grを
回収した。
[Photodegradability test conditions] 100W high-pressure mercury lamp temperature = 27°C 1% aqueous polymer electrolyte solution: 200ml [Molecular weight measurement conditions] GPC method column: 5hodex 0Hpak flow rate: 1 ml/min Column temperature: 40°C Eluent: 0 .05M-KC7! Aqueous solution [Comparative example] In a Hastelloy-C autoclave equipped with an induction stirrer and an external heater, 30 gr of maleic anhydride,
100 ml of a benzene solution containing 0.3 gr of "benzoylperoxy" was charged.The autoclave was then sealed, and the autoclave was replaced six times with 10 kg/c++ IC pressurized ethylene, and then G ethylene was introduced at 50 kg/c as calculated by pressure gauge. While stirring constantly, the temperature of the reaction mixture in the autoclave was adjusted to 70 ± 2°C using a heating heater, and the reaction was carried out for 4 hours.After that, the reactor was cooled and degassed, and then opened to form a slurry. I took out the slurry.
After adding to 00ml of ether, insoluble substances were filtered off, washed with ether, and dried to recover 22.3g of copolymer.

この共重合物に一定量の蒸留水を添加し、pH10の値
が保持されるまで、20重量%のNaOH水溶液を、添
加することによってこれを中和した。
A certain amount of distilled water was added to this copolymer and it was neutralized by adding a 20% by weight aqueous NaOH solution until a value of pH 10 was maintained.

無色透明な溶液が得られ、溶質濃度を一定に調節した後
、メタノール中にて処理すると、白色粉末の高分子電解
質を得た。
A colorless and transparent solution was obtained, and after adjusting the solute concentration to a constant value, the solution was treated in methanol to obtain a white powder of a polymer electrolyte.

高分子電解質は分析の結果、COを全く含まないマレイ
ン酸、エチレン共重合体である。光分解性試験結果を実
施例と共に表−1に示す。
As a result of analysis, the polymer electrolyte is a maleic acid and ethylene copolymer that does not contain any CO. The photodegradability test results are shown in Table 1 along with Examples.

[実施例−11 誘導撹拌機及び、外部加熱ヒーターを備えた、200m
1ハステロイ−C製オートクレーブを密封し、10kg
/c+aG加圧エチレンで6回置換した後、圧力計で4
0kg/an!Gのエチレンを導入し、次いで同様に1
00 kg/cJGの一酸化炭素を導入した。
[Example-11 200m equipped with induction stirrer and external heater
1. Seal the Hastelloy-C autoclave and store 10 kg.
/c+aG After replacing with pressurized ethylene 6 times, the pressure gauge shows 4
0kg/an! G of ethylene is introduced and then similarly 1
00 kg/cJG of carbon monoxide was introduced.

高圧定量ポンプを用いて、ベンゼン25m1を供給し、
一定の撹拌を行いながら、加熱用ヒーターでオートクレ
ーブ中の反応混合物の温度を70±2℃に調節した後、
無水マレイン酸15gr、ヘンシイルベルオキシド0.
750grを含むベンゼン溶液81、1 grを、高圧
定量ポンプを用い、0.113 gr/分の供給速度で
、12時間反応を行った。以下比較例と同様な方法、条
件で共重合物19.5grを回収し、ケン化処理後の高
分子電解質は、分析の結果、CO全含量8.0モル%で
あった。光分解性試験結果を比較例と共に表−1に示す
Using a high-pressure metering pump, supply 25 ml of benzene,
After adjusting the temperature of the reaction mixture in the autoclave to 70 ± 2 °C with a heating heater while performing constant stirring,
Maleic anhydride 15 gr, hensyl peroxide 0.
81.1 gr of a benzene solution containing 750 gr was reacted for 12 hours at a feed rate of 0.113 gr/min using a high-pressure metering pump. 19.5g of copolymer was recovered using the same method and conditions as in the comparative example, and analysis of the polymer electrolyte after saponification showed that the total CO content was 8.0 mol%. The photodegradability test results are shown in Table 1 along with comparative examples.

[実施例−2] 誘導撹拌機及び、外部加熱ヒーターを備えた、1100
mlハステロイ−C製オートクレーブを密封し、10k
g/c(G加圧エチレンで6回置換した後、圧力計で4
0kg/cfGのエチレンを導入し、次いで同様に10
0 kg/c++tGの一酸化炭素を導入した。高圧定
量ポンプを用いて、ベンゼン250m1を供給し、一定
の撹拌を行いながら加熱用ヒーターでオートクレーブ中
の反応混合物の温度を70±2℃に調節した後、無水マ
レイン酸75gr、ベンゾイルペルオキシド5.630
 grを含むベンゼン溶液414.4 grを、高圧定
量ポンプを用い、0.576gr/分の供給速度で、1
2時間反応を行った。以下比較例と同様な方法、条件で
共重合物100.7grを回収し、ケン化処理後の高分
子電解質は、分析の結果、CO全含量12.1モル%で
あった。光分解性試験結果を比較例と共に表−1に示す
[Example-2] 1100 equipped with an induction stirrer and an external heater
ml Hastelloy-C autoclave is sealed and 10k
g/c (G After replacing with pressurized ethylene 6 times, the pressure gauge shows 4
0 kg/cfG of ethylene was introduced and then similarly 10 kg/cfG of ethylene was introduced.
0 kg/c++tG of carbon monoxide was introduced. Using a high-pressure metering pump, 250 ml of benzene was supplied, and the temperature of the reaction mixture in the autoclave was adjusted to 70 ± 2°C with a heater while stirring constantly, and then 75 gr of maleic anhydride and 5.630 g of benzoyl peroxide were added.
414.4 gr of a benzene solution containing gr was added at a feed rate of 0.576 gr/min using a high-pressure metering pump to 1
The reaction was carried out for 2 hours. 100.7g of copolymer was recovered using the same method and conditions as in the comparative example, and analysis of the polymer electrolyte after saponification showed that the total CO content was 12.1 mol%. The photodegradability test results are shown in Table 1 along with comparative examples.

[表−1] 分子量二重量子均分子!(MW) 変化率i Mw (xhr) /Mw(Ohr)×10
0 [実施例−3] 実施例−2の高分子電解質を用いて光分解試験を行い、
試験前後の物質について生分解性試験を行った。試験条
件は化学物質審査規制法における方法により閉鎖系酸素
消費量測定装置を用いて行なった。200m1の基礎培
養基に試験物!50ppm下水処理活性汚泥1100p
pを調製し25℃で酸素消費量の変化を経時的に測定し
た。8時間光分解後の高分子電解質は、14日後の分解
率が50%と高い分解率を示すのに対して光分解を受け
ないものはほとんど分解されなかった。
[Table-1] Molecular weight double quantum uniform molecule! (MW) Rate of change i Mw (xhr) /Mw(Ohr)×10
0 [Example-3] A photolysis test was conducted using the polymer electrolyte of Example-2,
A biodegradability test was conducted on the material before and after the test. The test conditions were conducted using a closed system oxygen consumption measuring device in accordance with the method stipulated in the Chemical Substances Examination and Regulation Act. Test material in 200ml of basic culture medium! 50ppm sewage treatment activated sludge 1100p
p was prepared and the change in oxygen consumption was measured over time at 25°C. The polymer electrolyte photolyzed for 8 hours showed a high decomposition rate of 50% after 14 days, whereas the polymer electrolyte that did not undergo photolysis was hardly decomposed.

特許出願人  三菱油化株式会社Patent applicant: Mitsubishi Yuka Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 不飽和カルボン酸、オレフィン、一酸化炭素の共重合反
応で得られる重合体に波長2200〜6000オングス
トロームを有する光を照射する事を特徴とする、高分子
電解質の処理方法。
A method for treating a polymer electrolyte, comprising irradiating a polymer obtained by a copolymerization reaction of an unsaturated carboxylic acid, an olefin, and carbon monoxide with light having a wavelength of 2,200 to 6,000 angstroms.
JP22204688A 1988-09-05 1988-09-05 Treatment of polymer electrolyte Pending JPH0269523A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22204688A JPH0269523A (en) 1988-09-05 1988-09-05 Treatment of polymer electrolyte

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22204688A JPH0269523A (en) 1988-09-05 1988-09-05 Treatment of polymer electrolyte

Publications (1)

Publication Number Publication Date
JPH0269523A true JPH0269523A (en) 1990-03-08

Family

ID=16776247

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22204688A Pending JPH0269523A (en) 1988-09-05 1988-09-05 Treatment of polymer electrolyte

Country Status (1)

Country Link
JP (1) JPH0269523A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2008032679A1 (en) * 2006-09-11 2010-01-28 旭化成株式会社 POLYMER ELECTROLYTE, PROCESS FOR PRODUCING THE SAME, AND ELECTROCHEMICAL DEVICE

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49105891A (en) * 1973-01-16 1974-10-07
JPS49126800A (en) * 1973-04-04 1974-12-04

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49105891A (en) * 1973-01-16 1974-10-07
JPS49126800A (en) * 1973-04-04 1974-12-04

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2008032679A1 (en) * 2006-09-11 2010-01-28 旭化成株式会社 POLYMER ELECTROLYTE, PROCESS FOR PRODUCING THE SAME, AND ELECTROCHEMICAL DEVICE

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