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JPH02106915A - Electrolyte for driving electrolytic condenser and manufacture thereof - Google Patents

Electrolyte for driving electrolytic condenser and manufacture thereof

Info

Publication number
JPH02106915A
JPH02106915A JP26030788A JP26030788A JPH02106915A JP H02106915 A JPH02106915 A JP H02106915A JP 26030788 A JP26030788 A JP 26030788A JP 26030788 A JP26030788 A JP 26030788A JP H02106915 A JPH02106915 A JP H02106915A
Authority
JP
Japan
Prior art keywords
quaternary ammonium
electrolytic
aqueous solution
cation exchange
carboxylic 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.)
Granted
Application number
JP26030788A
Other languages
Japanese (ja)
Other versions
JP2739217B2 (en
Inventor
Noriki Ushio
潮 憲樹
Keiji Mori
啓治 森
Hideki Shimamoto
秀樹 島本
Hisao Nagara
久雄 長柄
Yukari Washio
鷲尾 由賀利
Yoshiteru Kuwae
桑江 良輝
Kazuji Shiono
塩野 和司
Takaaki Kishi
隆明 紀氏
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.)
Sanyo Chemical Industries Ltd
Panasonic Holdings Corp
Original Assignee
Sanyo Chemical Industries Ltd
Matsushita Electric Industrial 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 Sanyo Chemical Industries Ltd, Matsushita Electric Industrial Co Ltd filed Critical Sanyo Chemical Industries Ltd
Priority to JP26030788A priority Critical patent/JP2739217B2/en
Publication of JPH02106915A publication Critical patent/JPH02106915A/en
Application granted granted Critical
Publication of JP2739217B2 publication Critical patent/JP2739217B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

PURPOSE:To enhance the performance by electrolyzing unsymmetrical quaternary ammonium halide having a specified composition in an electrolytic bath making a cation exchange film a diaphragm, and by using carboxylic acid unsymmetrical quaternary ammonium salt synthesized with the aqueous solution of the unsymmetrical quaternary ammonium hydroxide obtained by the electrolysis and used as raw material. CONSTITUTION:Unsymmetrical quaternary ammonium halide shown by the equation is electrolyzed in an electrolytic bath with a cation exchange film used as a diaphragm, and unsymmetrical quaternary ammonium hydroxide is obtained. With its aqueous solution used as raw material, carboxylic acid, unsymmetrical quaternary ammonium salt is synthesized and used. In the equation, R1 expresses alkyl with a carbon number 1 to 4; R2 and R3 express alkyl with carbon numbers 2 to 4; and X expresses a halogen. Chloride, bromide, iodide, etc., are given as examples of halide. As examples of unsymmetrical quaternary ammonium triethyl methyl ammonium, triisopropyl methyl ammonium, etc., are given, and they are obtained by reacting alkyl halide and tertiary amine corresponding to their constitution with water used as a solvent.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、電解コンデンサ駆動用電解液およびその製造
方法に関する。さらに詳しくは、実質上ハロゲンを含ま
ない第四アンモニウム塩を電解質とした電解コンデンサ
駆動用電解液およびその製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an electrolytic solution for driving an electrolytic capacitor and a method for manufacturing the same. More specifically, the present invention relates to an electrolytic solution for driving an electrolytic capacitor using a substantially halogen-free quaternary ammonium salt as an electrolyte, and a method for manufacturing the same.

〔従来の技術] 従来、第四アンモニウム塩を使用する電解コンデンサ駆
動用電解液としてはテトラメチルアンモニウムクロライ
ド、テトラエチルアンモニウムクロライド、テトラブチ
ルアンモニウムクロライドなどの対称第四アンモニウム
ハライドを陽イオン交換膜を用いて電解し得られた第四
アンモニウムハイドロキサイド水溶液を使用する電解液
(特開昭63−80518号公報)が知られている。
[Prior Art] Conventionally, as an electrolytic solution for driving an electrolytic capacitor using a quaternary ammonium salt, a symmetrical quaternary ammonium halide such as tetramethylammonium chloride, tetraethylammonium chloride, or tetrabutylammonium chloride is used using a cation exchange membrane. An electrolytic solution (Japanese Unexamined Patent Publication No. 80518/1983) using a quaternary ammonium hydroxide aqueous solution obtained by electrolysis is known.

〔発明が解決しようとする問題点] しかしながら、従来の対称第四アンモニウムハライドの
電解により得られる第四アンモニウムハイドロキサイド
水溶液を使用する電解液は、第四アンモニウムがテトラ
エチルアンモニウム、テトライソプロピルアンモニウム
、テトラブチルアンモニウム等のメチル基より大きなア
ルキル基で構成されるものに適用した場合は、陽イオン
交換膜の抵抗が大きく、膜にブリスター(水膨れ現象)
が発生しやすく、摺電圧の上昇、電流効率の低下等の問
題が生じた。また第四アンモニウムハイドロキサイド水
溶液のハロゲンの除去率が充分でなく、それを使用した
電解液は高溶質濃度でコンデンサーの腐食や耐電圧の劣
化を引き起こす等の問題があった。
[Problems to be Solved by the Invention] However, in an electrolytic solution using a quaternary ammonium hydroxide aqueous solution obtained by conventional electrolysis of a symmetrical quaternary ammonium halide, the quaternary ammonium is tetraethylammonium, tetraisopropylammonium, or tetraethylammonium. When applied to a substance composed of an alkyl group larger than a methyl group such as butylammonium, the resistance of the cation exchange membrane is large and the membrane becomes blistered.
This caused problems such as an increase in sliding voltage and a decrease in current efficiency. Furthermore, the halogen removal rate of the quaternary ammonium hydroxide aqueous solution is not sufficient, and the electrolyte solution using it has problems such as high solute concentration, which causes corrosion of the capacitor and deterioration of the withstand voltage.

それ故、本発明の目的は電解コンデンサに使用される電
解液において、溶解性の高い第四アンモニウム塩とその
実質的にハロゲンを含まない製造方法により、これを使
用する高性能電解コンデンサを提供することにある。
Therefore, an object of the present invention is to provide a high-performance electrolytic capacitor using a quaternary ammonium salt having high solubility in an electrolyte used in an electrolytic capacitor, and a method for producing the quaternary ammonium salt substantially free of halogen. There is a particular thing.

c問題点を解決するための手段] 本発明者らは、上記問題点に鑑みて、実質上ハロゲンを
含まない高溶解性の第四アンモニウム塩およびその製造
方法を見い出すべく鋭意検討した結果、本発明に到達し
た。
c. Means for Solving the Problems] In view of the above problems, the present inventors have conducted intensive studies to find a highly soluble quaternary ammonium salt that does not substantially contain halogen and a method for producing the same, and as a result, the present inventors have developed the present invention. The invention has been achieved.

すなわち、本発明の電解コンデンサ駆動用電解液は、 
一般式(り (R+は炭素数1〜4のアルキル基を表し、R1、R3
は炭素数2〜4のアルキル基を表し、Xはハロゲンを表
す)で示される非対称第四アンモニウムハライドを、陽
イオン交換膜を隔膜とした電解槽で電解し、得られた非
対称第四アンモニウムハイドロキサイド水溶液を原料と
して合成したカルボン酸非対称第四アンモニウム塩を使
用することを特徴とする。
That is, the electrolytic solution for driving an electrolytic capacitor of the present invention is
General formula (R+ represents an alkyl group having 1 to 4 carbon atoms, R1, R3
represents an alkyl group having 2 to 4 carbon atoms and X represents a halogen) is electrolyzed in an electrolytic cell with a cation exchange membrane as a diaphragm, and the resulting asymmetric quaternary ammonium hydro It is characterized by using a carboxylic acid asymmetric quaternary ammonium salt synthesized from an aqueous oxide solution as a raw material.

ハライドの例としてはクロライド、ブロマイド、ヨーダ
イト等が挙げられるが、好ましくはクロライドである。
Examples of halides include chloride, bromide, iodite, etc., but chloride is preferred.

非対称第四アンモニウムの例としては、トリエチルメチ
ルアンモニウム、 トリイソプロピルメチルアンモニウ
ム、メチルトリブチルアンモニウム、メチルエチルジプ
チルアンモニウム、ジエチルジメチルアンモニウム、ジ
メチルジイソプロピルアンモニウム、ジブチルジメチル
アンモニウムチルジメチルイソプロピルアンモニウム等
が挙げられる。これらの内好ましくは、 トリエチルメ
チルアンモニウム、トリイソプロピルメチルアンモニウ
ム、ジエチルジメチルアンモニウム、ジメチルジイソプ
ロピルアンモニウム、ジブチルジメチルアンモニウムで
ある。更に好ましくはトリエチルメチルアンモニウムお
よびジエチルジメチルアンモニウムである。
Examples of asymmetric quaternary ammoniums include triethylmethylammonium, triisopropylmethylammonium, methyltributylammonium, methylethyldiptylammonium, diethyldimethylammonium, dimethyldiisopropylammonium, dibutyldimethylammonium, tildimethylisopropylammonium, and the like. Among these, preferred are triethylmethylammonium, triisopropylmethylammonium, diethyldimethylammonium, dimethyldiisopropylammonium, and dibutyldimethylammonium. More preferred are triethylmethylammonium and diethyldimethylammonium.

これらの非対称第四アンモニウムハライドは、その構造
に対応する3級アミンとアルキルハライドを、水を溶媒
として反応させることにより得ることができる。例えば
、 トリエチルメチルアンモニウムクロライドは、ガラ
スオートクレーブ中に、トリエチルアミン33.5重量
部、イオン交換水50ffiffi部を仕込み温度的6
0℃、圧力5kg/cm”Gの条件でメチルクロライド
17.5mff1部を数時間で吹き込んで4級化反応を
行った後、窒素などを吹き込むか@減圧として過剰のメ
チルクロライドを除去する方法で509A水溶液がほぼ
定m的に得られる。
These asymmetric quaternary ammonium halides can be obtained by reacting a tertiary amine corresponding to the structure with an alkyl halide using water as a solvent. For example, triethylmethylammonium chloride is prepared by placing 33.5 parts by weight of triethylamine and 50 ffiffi parts of ion-exchanged water in a glass autoclave.
After carrying out a quaternization reaction by blowing 1 part of methyl chloride into the reaction mixture over several hours at 0°C and a pressure of 5 kg/cm"G, excess methyl chloride is removed by blowing in nitrogen or the like or by reducing the pressure. A 509A aqueous solution is obtained almost constantly.

カルボン酸非対称第四アンモニウム塩を形成するカルボ
ン酸の例としては、マレイン酸、シトラコン酸、テトラ
ヒドロフタル酸等の不飽和脂肪族カルボン酸、フタル酸
、安息香酸等の芳香族カルボン酸、ヘキサヒドロフタル
酸等の脂環式脂肪族カルボン酸、酢酸、プロピオン酸等
の脂肪族モノカルボン酸、マロン酸、コハク酸、アジピ
ン酸、アゼライン酸およびデカンジカルボン酸等の飽和
脂肪族ジカルボン酸等が挙げられる。
Examples of carboxylic acids that form carboxylic acid asymmetric quaternary ammonium salts include unsaturated aliphatic carboxylic acids such as maleic acid, citraconic acid, and tetrahydrophthalic acid; aromatic carboxylic acids such as phthalic acid and benzoic acid; and hexahydrophthalic acid. Examples include alicyclic aliphatic carboxylic acids such as acids, aliphatic monocarboxylic acids such as acetic acid and propionic acid, and saturated aliphatic dicarboxylic acids such as malonic acid, succinic acid, adipic acid, azelaic acid and decanedicarboxylic acid.

カルボン酸非対称第四アンモニウム塩を溶解し電解液を
形成させる溶媒としては、γ−ブチロラクトン等のラク
トン類、プロピレンカーボネート等のカーボネート類、
DMF等のアミド類、アセトニトリル等のニトリル類、
エチレングリコール、エチルセロソルブ等のアルコール
類、スルホラン、ジメチルスルホキシド、N−メチルピ
ロリドン、3−メチル−1,3−オキサゾリジン−2−
オン、■、3−ジメチルー2−イミダゾリジノン等が挙
げられる。これらの内好ましくは、γ−ブチロラクトン
および、γ−プチロラクトンに50重量%以内の全で前
記の溶媒類を混合した混合溶媒である。
As the solvent for dissolving the asymmetric quaternary ammonium carboxylic acid salt to form an electrolytic solution, lactones such as γ-butyrolactone, carbonates such as propylene carbonate,
Amides such as DMF, nitriles such as acetonitrile,
Alcohols such as ethylene glycol and ethyl cellosolve, sulfolane, dimethyl sulfoxide, N-methylpyrrolidone, 3-methyl-1,3-oxazolidine-2-
1, 3-dimethyl-2-imidazolidinone and the like. Among these, preferred are γ-butyrolactone and a mixed solvent in which γ-butyrolactone is mixed with the above-mentioned solvents in a total amount of up to 50% by weight.

[実施例] 以下、実施例により本発明を更に説明するが、本発明は
これに限定されるものではない。以下において、%は重
量%を示す。
[Examples] Hereinafter, the present invention will be further explained with reference to Examples, but the present invention is not limited thereto. In the following, % indicates weight %.

実施例1 マレイン酸トリエチルメチルアンモニウムの調製 陽イオン交換膜としてデュポン社製ナフィオン膜324
を使用して電解禮をステンレス陰極の陰極室と白金めっ
きされたチタン陽極の陽極室に隔離L、35%トリエチ
ルメチルアンモニウムクロライド水溶液を循環し、陰極
室に2%トリエチルメチルアンモニウムハイドロキサイ
ド水溶液を循環して電流密度10〜2OA/dm2で電
解し、陰極室に粗25%メチルトリチルアンモニウムハ
イドロキサイド水溶液を得た。このものの塩素濃度は、
190pI)mであり、電流効率は76%であった。さ
らに同様の電解装置を用いて、陽極室に上で得られた粗
25%トリエチルメチルアンモニウムハイドロキサイド
水溶液を循環し、陰極室に2%トリエチルメチルアンモ
ニウムハイドロキサイド水溶液を循環し同様の電流密度
で電解し、陰極室に高純度20%トリエチルメチルアン
モニウムハイドロキサイド水溶液を得た。このものの塩
素濃度は2ppmであった。この電解操作による陽イオ
ン交換膜の異常は生じなかった。これを、採取して当モ
ルのマレイン酸を加え、減圧乾燥してマレイン酸トリエ
チルメチルアンモニウムとした。この塩のγ−ブチロラ
クトンに対する溶解性は25”Cで濃度50%以上であ
った。
Example 1 Preparation of triethylmethylammonium maleate Nafion membrane 324 manufactured by DuPont as a cation exchange membrane
The electrolysis was separated into a cathode chamber with a stainless steel cathode and an anode chamber with a platinum-plated titanium anode. A 35% triethylmethylammonium chloride aqueous solution was circulated, and a 2% triethylmethylammonium hydroxide aqueous solution was added to the cathode chamber. The mixture was circulated for electrolysis at a current density of 10 to 2 OA/dm2 to obtain a crude 25% aqueous methyltritylammonium hydroxide solution in the cathode chamber. The chlorine concentration of this substance is
The current efficiency was 76%. Furthermore, using the same electrolytic device, the crude 25% triethylmethylammonium hydroxide aqueous solution obtained above was circulated in the anode chamber, and the 2% triethylmethylammonium hydroxide aqueous solution was circulated in the cathode chamber to maintain the same current density. Electrolysis was performed to obtain a highly purified 20% triethylmethylammonium hydroxide aqueous solution in the cathode chamber. The chlorine concentration of this product was 2 ppm. No abnormality occurred in the cation exchange membrane due to this electrolytic operation. This was collected, added with the same molar amount of maleic acid, and dried under reduced pressure to obtain triethylmethylammonium maleate. The solubility of this salt in γ-butyrolactone was 50% or more at 25"C.

実施例2 マレイン酸トリイソプロピルメチルアンモニウムの調製 実施例1のトリエチルメチルアンモニウムクロライドの
代わりにトリイソプロピルメチルアンモニウムクロライ
ドを使用する以外は同様に実施して↑l125%トリイ
ソプロピルメチルアンモニウムハイドロキサイド水溶液
を得た。このものの塩素濃度は2601)1)mであり
、電流効率は72%であった。続いて同様に実施して高
純度20%トリイソプロピルメチルアンモニウムハイド
ロキサイド水溶液を得た。このものの塩素濃度は3pp
mであった。この電解操作による陽イオン交換膜の異常
は生じなかった。更に同様に実施してマレイン酸トリイ
ソプロピルメチルアンモニウムを得た。
Example 2 Preparation of triisopropylmethylammonium maleate A 125% aqueous solution of triisopropylmethylammonium hydroxide was obtained in the same manner as in Example 1 except that triisopropylmethylammonium chloride was used instead of triethylmethylammonium chloride. Ta. The chlorine concentration of this product was 2601)1)m, and the current efficiency was 72%. Subsequently, a highly purified 20% triisopropylmethylammonium hydroxide aqueous solution was obtained in the same manner. The chlorine concentration of this product is 3pp.
It was m. No abnormality occurred in the cation exchange membrane due to this electrolytic operation. Further, triisopropylmethylammonium maleate was obtained in the same manner.

この塩のγ−ブチロラクトンに対する溶解性は25°C
で濃度50%以上であった。
The solubility of this salt in γ-butyrolactone is 25°C.
The concentration was 50% or more.

実施例3 マレイン酸ジエチルジメチルアンモニウムの調製 実施例1のトリエチルメチルアンモニウムクロライドの
代わりにジエチルジメチルアンモニウムクロライドを使
用する以外は、同様に実施して粗25%ジエチルジメチ
ルアンモニウムハイドロキサイド水溶液を得た。このも
のの塩素濃度は140ppmであり、電流効率は84%
であった。この電解操作による陽イオン交換膜の異常は
生じなかった。続いて同様に実施して高純度20%ジエ
チルジメチルアンモニウムハイドロキサイド水溶液を得
た。このものの塩素濃度は2ppmであった。更に同様
に実施してマレイン酸ジエチルジメチルアンモニウムを
得た。この塩のγ−ブチロラクトンに対する溶解性は2
5°Cで500A以上であった。
Example 3 Preparation of diethyldimethylammonium maleate A crude 25% diethyldimethylammonium hydroxide aqueous solution was obtained in the same manner as in Example 1, except that diethyldimethylammonium chloride was used in place of triethylmethylammonium chloride. The chlorine concentration of this product is 140 ppm, and the current efficiency is 84%.
Met. No abnormality occurred in the cation exchange membrane due to this electrolytic operation. Subsequently, a high purity 20% diethyldimethylammonium hydroxide aqueous solution was obtained in the same manner. The chlorine concentration of this product was 2 ppm. Furthermore, diethyldimethylammonium maleate was obtained in the same manner. The solubility of this salt in γ-butyrolactone is 2
It was over 500A at 5°C.

実施例4 フタル酸トリエチルメチルアンモニウムの調製実施例1
でマレイン酸の代わりにフタル酸を使用する以外は同様
に実施して、フタル酸トリエチルメチルアンモニウムを
得た。この塩のγ−ブチロラクトンに対する溶解性は2
5℃で50%以上であった。
Example 4 Preparation of triethylmethylammonium phthalate Example 1
Triethylmethylammonium phthalate was obtained in the same manner except that phthalic acid was used instead of maleic acid. The solubility of this salt in γ-butyrolactone is 2
It was 50% or more at 5°C.

実施例5 フタル酸トリイソプロピルメチルアンモニウムの調製 実Ll+11でトリエチルメチルアンモニウムクロライ
ドの代わりにトリインプロピルメチルアンモニウムクロ
ライドを使用し、マレイン酸の代わりにフタル酸を使用
する以外は同様に実施して、フタル酸トリイソプロピル
メチルアンモニウムを得た。この塩のγ−ブチロラクト
ンに対する溶解性は25°Cで50%以上であった。
Example 5 Preparation of triisopropylmethylammonium phthalate The same procedure was repeated except that triisopropylmethylammonium chloride was used instead of triethylmethylammonium chloride in Example Ll+11, and phthalic acid was used instead of maleic acid. Triisopropylmethylammonium acid was obtained. The solubility of this salt in γ-butyrolactone was 50% or more at 25°C.

実施例6 フタル酸ジエチルジメチルアンモニウムの調製実施例1
でトリエチルメチルアンモニウムクロライドの代わりに
ジエチルジメチルアンモニウムクロライドを使用し、マ
レイン酸の代わりにフタル酸を使用する以外は同様に実
施して、フタル酸ジエチルジメチルアンモニウムを得た
。この塩のγ−ブチロラクトンに対する溶解性は25℃
で50%以上であった。
Example 6 Preparation of diethyldimethylammonium phthalate Example 1
Diethyldimethylammonium phthalate was obtained by carrying out the same procedure except that diethyldimethylammonium chloride was used instead of triethylmethylammonium chloride and phthalic acid was used instead of maleic acid. The solubility of this salt in γ-butyrolactone is 25°C.
It was more than 50%.

従来例1 マレイン酸テトラメチルアンモニウムの調製実施例1の
トリエチルメチルアンモニウムクロライドの代わりにテ
トラメチルアンモニウムクロライドを使用する以外は同
様に実施して、粗25%テトラメチルアンモニウムハイ
ドロキサイド水溶液を得た。このものの塩素含徂は12
0ppmであり電流効率は87%であった。この電解操
作による陽イオン交換膜の異常は生じなかった。続いて
同様に実施して直線度20%テトラメチルアンモニウム
ハイドロキサイド水溶液を得た。このものの塩素濃度は
Oo−3ppであった。更に同様にしてマレイン酸テト
ラメチルアンモニウムを得た。この塩のγ−ブチロラク
トンに対する溶解性は、25°Cで10%以下であった
Conventional Example 1 Preparation of Tetramethylammonium Maleate A crude 25% aqueous solution of tetramethylammonium hydroxide was obtained in the same manner as in Example 1 except that tetramethylammonium chloride was used instead of triethylmethylammonium chloride. The chlorine content of this product is 12
The current efficiency was 87%. No abnormality occurred in the cation exchange membrane due to this electrolytic operation. Subsequently, the same procedure was carried out to obtain a tetramethylammonium hydroxide aqueous solution with a linearity of 20%. The chlorine concentration of this product was Oo-3 pp. Furthermore, tetramethylammonium maleate was obtained in the same manner. The solubility of this salt in γ-butyrolactone was less than 10% at 25°C.

従来例2 フタル酸テトラメチルアンモニウムの調製実施例1でト
リエチルメチルアンモニウムクロライドの代わりにテト
ラメチルアンモニウムクロライドを使用し、マレイン酸
の代わりにフタル酸を使用する以外は同様に実施して、
フタル酸テトラメチルアンモニウムを得た。この塩のγ
−ブチロラクトンに対する溶解性は25°Cで30%以
下であった。
Conventional Example 2 Preparation of Tetramethylammonium Phthalate The same procedure as in Example 1 was carried out except that tetramethylammonium chloride was used instead of triethylmethylammonium chloride and phthalic acid was used instead of maleic acid.
Tetramethylammonium phthalate was obtained. γ of this salt
- Solubility in butyrolactone was less than 30% at 25°C.

従来例3 テトラエチルアンモニウムハイドロキサイド水溶液の調
製 実施例1のトリエチルメチルアンモニウムクロライドの
代わりにテトラエチルアンモニウムクロライドを使用す
る以外は同様に実施し、粗25%テトラエチルアンモニ
ウムハイドロキサイド水溶液を得た。このものの塩素濃
度は450ppmであり、電流効率は51%であった。
Conventional Example 3 Preparation of aqueous tetraethylammonium hydroxide solution A crude 25% aqueous solution of tetraethylammonium hydroxide was obtained in the same manner as in Example 1 except that tetraethylammonium chloride was used instead of triethylmethylammonium chloride. The chlorine concentration of this product was 450 ppm, and the current efficiency was 51%.

この電解操作により陽イオン交換膜にブリスター(水膨
れ)が生じたため、以後の操作を続けることはできなか
った。
This electrolytic operation caused blisters on the cation exchange membrane, so subsequent operations could not be continued.

従来例4 テトライソプロピルアンモニウムハイドロキサイド水溶
液の調製 実施例1のトリエチルメチルアンモニウムクロッ イトの代わりにテトライソプ口ピルアンモニウムクロラ
イドを使用する以外は同様に実施し、粗25%テトライ
ソプロピルアンモニウムノ)イドロキサイド水溶液を得
た。このものの塩素濃度は510ppmであり、?T!
流効率は41%であった。この電解操作により陽イオン
交換膜にブリスター(水膨れ)が生じたため、以後の操
作を続けることはできなかった。
Conventional Example 4 Preparation of an aqueous solution of tetraisopropylammonium hydroxide A crude 25% aqueous solution of tetraisopropylammonium hydroxide was prepared in the same manner as in Example 1 except that tetraisopropylammonium chloride was used instead of triethylmethylammonium clot. Obtained. The chlorine concentration of this product is 510 ppm. T!
The flow efficiency was 41%. This electrolytic operation caused blisters on the cation exchange membrane, so subsequent operations could not be continued.

実施例7 電解により高純度の第四アンモニウム塩を得ることがで
きた実施例1〜3および従来例1において得られたマレ
イン酸第四アンモニウム塩を、γ−ブチロラクトンに溶
解し比電導度の最大値が得られる濃度に調製した。これ
らの電解液の塩素含量はすべて5ppm以下であった。
Example 7 The quaternary ammonium maleate salts obtained in Examples 1 to 3 and Conventional Example 1, in which highly purified quaternary ammonium salts could be obtained by electrolysis, were dissolved in γ-butyrolactone to obtain the maximum specific conductivity. The concentration was adjusted to obtain the desired value. The chlorine content of these electrolytes was all 5 ppm or less.

得られた電解液の比電導度とその濃度を表1に示す。Table 1 shows the specific conductivity and concentration of the obtained electrolytic solution.

表1 [発明の効果コ 本発明のメチル基を1つ以上、2つ以内含ませた非対称
第四アンモニウムノ1ライドは、電解時に陽イオン交換
膜を傷つけることなく低電圧、高電流効率で電解するこ
とを可能にし、得られた第四アンモニウムハイドロキサ
イド水溶液を更に再度電解する方法や電解槽として3室
型槽を用いる方法等で、ハロゲンの除去率を向上させる
ことが容易である。また、前記非対称第四アンモニウム
ノ1ライドは、製造時にアルコール等の非水溶媒を必要
とせず水溶液で得られるため溶媒置換の必要がなく、そ
のまま電解に供することができるとともに、を機溶媒の
混入による若色物の発生や、電極金属の溶出等がない。
Table 1 [Effects of the Invention] The asymmetric quaternary ammonium nitride containing one or more but not more than two methyl groups of the present invention can be electrolyzed at low voltage and with high current efficiency without damaging the cation exchange membrane during electrolysis. It is easy to improve the halogen removal rate by further electrolyzing the obtained quaternary ammonium hydroxide aqueous solution or using a three-chamber tank as an electrolytic tank. In addition, the asymmetric quaternary ammonium nitride does not require a non-aqueous solvent such as alcohol during production and can be obtained as an aqueous solution, so there is no need for solvent replacement and it can be directly subjected to electrolysis. There is no generation of young colored matter or elution of electrode metal.

こうして得られた非対称第四アンモニウムハイドロキサ
イド水溶液を原料として合成したカルボン酸非対称第四
アンモニウム塩は実質上ハロゲンを含有せず、銀、アル
カリ金属も含量しないことからコンデンサーの腐食、シ
ョート等の問題がない。また、無機アニオンの非対称第
四アンモニウム塩やカルボン酸対称第四アンモニウム塩
に比較して溶解性が高まり、高濃度にすることで高電導
度を得ることができる。
The carboxylic acid asymmetric quaternary ammonium salt synthesized using the asymmetric quaternary ammonium hydroxide aqueous solution obtained as a raw material contains virtually no halogen, nor does it contain silver or alkali metals, which causes problems such as corrosion of capacitors and short circuits. There is no. In addition, the solubility is increased compared to an asymmetric quaternary ammonium salt of an inorganic anion or a symmetric quaternary ammonium salt of a carboxylic acid, and high conductivity can be obtained by increasing the concentration.

従って本発明によれば実質的にハロゲンを含まず、かつ
高溶解性のカルボン酸第四アンモニウム塩が製造され、
これにより腐食性がなく、高電導度を有し、高温安定性
、低温安定性に優れた電解コンデンサ駆動用電解液が提
供できる。
Therefore, according to the present invention, a substantially halogen-free and highly soluble carboxylic acid quaternary ammonium salt is produced,
This makes it possible to provide an electrolytic solution for driving an electrolytic capacitor that is non-corrosive, has high conductivity, and has excellent high-temperature stability and low-temperature stability.

Claims (3)

【特許請求の範囲】[Claims] 1.一般式(I) ▲数式、化学式、表等があります▼(I) (R_1は炭素数1〜4のアルキル基を表し、R_2、
R_3は炭素数2〜4のアルキル基を表し、Xはハロゲ
ンを表す)で示される非対称第四アンモニウムハライド
を、陽イオン交換膜を隔膜とした電解槽で電解し、得ら
れた非対称第四アンモニウムハイドロキサイド水溶液を
原料として合成したカルボン酸非対称第四アンモニウム
塩を使用することを特徴とする電解コンデンサ駆動用電
解液。
1. General formula (I) ▲Mathematical formulas, chemical formulas, tables, etc.▼(I) (R_1 represents an alkyl group having 1 to 4 carbon atoms, R_2,
R_3 represents an alkyl group having 2 to 4 carbon atoms, X represents a halogen) is electrolyzed in an electrolytic cell with a cation exchange membrane as a diaphragm, and the resulting asymmetric quaternary ammonium An electrolytic solution for driving an electrolytic capacitor characterized by using an asymmetric quaternary ammonium carboxylic acid salt synthesized from an aqueous hydroxide solution as a raw material.
2.非対称第四アンモニウムが、トリエチルメチルアン
モニウム、トリイソプロピルメチルアンモニウム、ジエ
チルジメチルアンモニウム、ジメチルジイソプロピルア
ンモニウム、ジブチルジメチルアンモニウムである特許
請求の範囲第1項記載の電解コンデンサ駆動用電解液。
2. The electrolytic solution for driving an electrolytic capacitor according to claim 1, wherein the asymmetric quaternary ammonium is triethylmethylammonium, triisopropylmethylammonium, diethyldimethylammonium, dimethyldiisopropylammonium, or dibutyldimethylammonium.
3.一般式(I) ▲数式、化学式、表等があります▼(I) (R_1は炭素数1〜4のアルキル基を表し、R_2、
R_3は炭素数2〜4のアルキル基を表し、Xはハロゲ
ンを表す)で示される非対称第四アンモニウムハライド
を、陽イオン交換膜を隔膜とした電解槽で電解し、得ら
れた非対称第四アンモニウムハイドロキサイド水溶液を
カルボン酸と反応させ、カルボン酸非対称第四アンモニ
ウム塩を製造することを特徴とする電解コンデンサ駆動
用電解液の製造方法。
3. General formula (I) ▲Mathematical formulas, chemical formulas, tables, etc.▼(I) (R_1 represents an alkyl group having 1 to 4 carbon atoms, R_2,
R_3 represents an alkyl group having 2 to 4 carbon atoms, X represents a halogen) is electrolyzed in an electrolytic cell with a cation exchange membrane as a diaphragm, and the resulting asymmetric quaternary ammonium A method for producing an electrolytic solution for driving an electrolytic capacitor, which comprises reacting an aqueous hydroxide solution with a carboxylic acid to produce an asymmetric quaternary ammonium salt of a carboxylic acid.
JP26030788A 1988-10-15 1988-10-15 Electrolytic solution for driving electrolytic capacitor and method for producing the same Expired - Lifetime JP2739217B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5523487A (en) * 1993-06-09 1996-06-04 Lonza, Inc. Quaternary ammonium carbonate compositions and preparation thereof
US5700841A (en) * 1993-06-09 1997-12-23 Lonza Inc. Quaternary ammonium carboxylate and borate compositions and preparation thereof
JP2009161537A (en) * 2001-05-11 2009-07-23 Mitsubishi Chemicals Corp Organic onium tetrafluoroaluminate and production method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5523487A (en) * 1993-06-09 1996-06-04 Lonza, Inc. Quaternary ammonium carbonate compositions and preparation thereof
US5700841A (en) * 1993-06-09 1997-12-23 Lonza Inc. Quaternary ammonium carboxylate and borate compositions and preparation thereof
US6090855A (en) * 1993-06-09 2000-07-18 Lonza, Inc. Quaternary ammonium carbonate compositions and preparation thereof
JP2009161537A (en) * 2001-05-11 2009-07-23 Mitsubishi Chemicals Corp Organic onium tetrafluoroaluminate and production method thereof
JP4631975B2 (en) * 2001-05-11 2011-02-16 三菱化学株式会社 Electrolytic solution for electrolytic capacitor and electrolytic capacitor having the same

Also Published As

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