JP2012134550A - Aluminum electrolytic capacitor electrolyte and manufacturing method for core solute thereof - Google Patents

Aluminum electrolytic capacitor electrolyte and manufacturing method for core solute thereof Download PDF

Info

Publication number
JP2012134550A
JP2012134550A JP2012070588A JP2012070588A JP2012134550A JP 2012134550 A JP2012134550 A JP 2012134550A JP 2012070588 A JP2012070588 A JP 2012070588A JP 2012070588 A JP2012070588 A JP 2012070588A JP 2012134550 A JP2012134550 A JP 2012134550A
Authority
JP
Japan
Prior art keywords
branched chain
dicarboxylic acid
acid containing
solvent
carbon atoms
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
JP2012070588A
Other languages
Japanese (ja)
Other versions
JP5466256B2 (en
Inventor
Zheng Zhongtian
鄭仲天
He Tianqian
何天虔
Chen Changchun
陳長春
Xiang Qiufen
向秋芬
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.)
Shenzhen Capchem Technology Co Ltd
Original Assignee
Shenzhen Capchem Technology 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 Shenzhen Capchem Technology Co Ltd filed Critical Shenzhen Capchem Technology Co Ltd
Publication of JP2012134550A publication Critical patent/JP2012134550A/en
Application granted granted Critical
Publication of JP5466256B2 publication Critical patent/JP5466256B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Secondary Cells (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an aluminum electrolytic capacitor electrolyte and a manufacturing method for its core solute, and especially a mid-to-high voltage aluminum electrolytic capacitor electrolyte having high thermal stability.SOLUTION: An aluminum electrolytic capacitor electrolyte containing a solvent and a solute is provided, the solute containing dicarboxylic acid including a branched chain in α position or a salt thereof and the solvent being a mixed solvent composed of one kind or two kinds or more selected from alcohol-, alcohol ether-, amid-, sulfone-, sulfoxide- and ester-system solvents, characterized in that the content of dicarboxylic acid including a branched chain in α position or a salt thereof is 0.1-30 mass%, preferably 2.5-15 mass%, in terms of dicarboxylic acid including a branched chain in α position. In addition, a manufacturing method for dicarboxylic acid including a branched chain in α position and an ammonium salt thereof is provided. An electrolyte derived from dicarboxylic acid including a branched chain in α position and a salt thereof exhibit still better solubility and thermal stability in ethylene glycol. An obtained capacitor is advantageous in that it has a long life and excels in low temperature performance.

Description

本発明は、アルミニウム電解コンデンサの電解液及びその核心溶質の製造方法に関して、特に、中高圧アルミニウム電解コンデンサの電解液及びその核心溶質の製造方法に関する。   The present invention relates to an electrolytic solution for an aluminum electrolytic capacitor and a method for producing the core solute thereof, and more particularly, to an electrolytic solution for a medium-high pressure aluminum electrolytic capacitor and a method for producing the core solute.

従来、中高圧アルミニウム電解コンデンサの電解液は、主溶媒としてエチレングリコールが使用され、主溶質としてホウ酸又は五ホウ酸アンモニウム等の無機化合物が使用された。このような電解液に、導電率が低い問題点があり、その後、電解液主溶質として、アゼライン酸、セバシン酸、ドデカン二酸等の直鎖状二酸またはそれらのアンモニウム塩等に替えて用いられ、さらに、以上の無機塩と以上のような有機酸を配合して溶質とすることもあるが、このような電解液は、高温熱安定性が悪い問題点がある。高温で長期にわたってその導電率が大幅に低下するため、コンデンサの抵抗値が上昇しコンデンサの寿命に悪い影響を及ぼしてしまう。そのなか、ホウ酸又はその塩は、高温でエチレングリコールと反応して水を生成するので、コンデンサの寿命に悪い影響を及ぼし、それに、セバシン酸アンモニウム、ドデカン二酸アンモニウム及びその酸は、エチレングリコールに室温で6%未満ほど低い溶解性を有するので、アルミニウム電解コンデンサの低温性能を劣化させる。   Conventionally, in an electrolytic solution of a medium / high pressure aluminum electrolytic capacitor, ethylene glycol is used as a main solvent, and an inorganic compound such as boric acid or ammonium pentaborate is used as a main solute. Such electrolytes have the problem of low electrical conductivity, and then used as the electrolyte main solute instead of linear diacids such as azelaic acid, sebacic acid, dodecanedioic acid or their ammonium salts. In addition, the above inorganic salt and the above organic acid may be blended to form a solute, but such an electrolytic solution has a problem of poor high-temperature thermal stability. Since the conductivity of the capacitor greatly decreases over a long period of time at a high temperature, the resistance value of the capacitor rises and adversely affects the life of the capacitor. Among them, boric acid or a salt thereof reacts with ethylene glycol at a high temperature to produce water, thus adversely affecting the life of the capacitor. Furthermore, it has a solubility as low as less than 6% at room temperature, which degrades the low temperature performance of the aluminum electrolytic capacitor.

本発明の第1の目的は、今のアルミニウム電解コンデンサ電解液の高温熱安定性が悪く、高温導電率が低いことについて、高い熱安定性を有する中高圧アルミニウム電解コンデンサ用電解液を提供することである。   The first object of the present invention is to provide an electrolytic solution for medium- and high-pressure aluminum electrolytic capacitors, which has high thermal stability with respect to the poor high-temperature thermal stability of the current aluminum electrolytic capacitor electrolyte and low high-temperature conductivity. It is.

本発明の第2の目的は、前述電解液の核心溶質の製造方法を提供することである。   The second object of the present invention is to provide a method for producing the core solute of the electrolyte.

本発明の第1の目的は、次のような技術によって達成される。   The first object of the present invention is achieved by the following technique.

溶媒と溶質を含むアルミニウム電解コンデンサ電解液であって、前記溶質は、α位に分枝鎖を含有するジカルボン酸或いはその塩を含み、前記溶媒は、アルコール系、アルコールエーテル系、アミド系、スルホン系、スルホキシド系、及びエステル系の溶媒から選ばれる一種又は二種以上から形成する混合溶媒であり、かつ、その中、α位に分枝鎖を含有するジカルボン酸或いはその塩の含有量は、α位に分枝鎖を含有するジカルボン酸で、0.1〜30質量%、好ましくは2.5〜15質量%であることを特徴とするアルミニウム電解コンデンサ電解液が提供される。   An electrolytic solution of an aluminum electrolytic capacitor containing a solvent and a solute, wherein the solute contains a dicarboxylic acid containing a branched chain at the α-position or a salt thereof, and the solvent is an alcohol, alcohol ether, amide, sulfone Is a mixed solvent formed from one or two or more types selected from solvents of the type, sulfoxide type, and ester type, and among them, the content of the dicarboxylic acid or salt thereof containing a branched chain at the α-position is: An aluminum electrolytic capacitor electrolyte characterized in that it is 0.1 to 30% by mass, preferably 2.5 to 15% by mass, of a dicarboxylic acid containing a branched chain at the α-position.

好ましく、前記α位に分枝鎖を含有するジカルボン酸は、次の化学式1(化1)を有する。
(上式中、R1は炭素数1〜20の炭化水素基又は水素原子を表し、この炭化水素基は、直鎖状又は分枝鎖状であってもよく、飽和又は不飽和であってもよい。また、主鎖及び分枝鎖には、エーテル基、エステル基、シアノ基、アミド基、ヒドロキシ基、カルボキシル基等を含んでもよい。
R2は炭素数1〜20の炭化水素基を表し、この炭化水素基は、直鎖状又は分枝鎖状であってもよく、飽和又は不飽和であってもよい。また、主鎖と分枝鎖に、エーテル基、エステル基、シアノ基、アミド基、ヒドロキシル基、又はカルボキシル基等を含んでもよい。
nは2〜15の整数である。)
Preferably, the dicarboxylic acid containing a branched chain at the α-position has the following chemical formula 1 (Formula 1).
(In the above formula, R 1 represents a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom, and this hydrocarbon group may be linear or branched, saturated or unsaturated, In addition, the main chain and the branched chain may contain an ether group, an ester group, a cyano group, an amide group, a hydroxy group, a carboxyl group, and the like.
R 2 represents a hydrocarbon group having 1 to 20 carbon atoms, and this hydrocarbon group may be linear or branched, and may be saturated or unsaturated. Further, the main chain and the branched chain may include an ether group, an ester group, a cyano group, an amide group, a hydroxyl group, or a carboxyl group.
n is an integer of 2-15. )

好ましく、前記α位に分枝鎖を含有するジカルボン酸塩とは、α位に分枝鎖を含有するジカルボン酸とアンモニア又はアミンから形成する塩である。   Preferably, the dicarboxylate containing a branched chain at the α-position is a salt formed from a dicarboxylic acid containing a branched chain at the α-position and ammonia or an amine.

好ましく、前記溶媒は、エチレングリコール又はγ−ブチロラクトンから選ばれる一種又は二種の混合物である。   Preferably, the solvent is one or a mixture of two selected from ethylene glycol or γ-butyrolactone.

好ましく、前記電解液に、さらに、次亜リン酸、亜リン酸、リン酸、リン酸モノアルキルエーテル、或いはそれらのアンモニア又はアミン塩から選ばれる少なくとも一種のものを含んでもよく、また、それらの総含有量が0.05〜5質量%、好ましくは0.1〜3質量%である。   Preferably, the electrolyte solution may further contain at least one selected from hypophosphorous acid, phosphorous acid, phosphoric acid, phosphoric acid monoalkyl ether, or ammonia or an amine salt thereof, The total content is 0.05 to 5% by mass, preferably 0.1 to 3% by mass.

好ましく、前記電解液に、さらに、p−ニトロフェノール、p−ニトロベンジルアルコール、o−ニトロアニソール、m−ニトロアセトフェノン、p−ニトロベンゼンカルボン酸等のニトロ化合物から選ばれる一種又は二種以上の混合物を含んでもよく、また、それらの総含有量が0.05〜15質量%、好ましくは0.1〜4質量%である。   Preferably, the electrolyte solution further includes one or a mixture of two or more selected from nitro compounds such as p-nitrophenol, p-nitrobenzyl alcohol, o-nitroanisole, m-nitroacetophenone, and p-nitrobenzenecarboxylic acid. The total content thereof may be 0.05 to 15% by mass, preferably 0.1 to 4% by mass.

好ましく、前記電解液に、さらに、他の有機酸又はそのアンモニウム塩、例えば、ホウ酸又は五ホウ酸アンモニウム、セバシン酸、アゼライン酸、ベンゼンカルボン酸、アジピン酸、ドデカン二酸、1,6−ドデカン二酸、1,7−セバシン酸から選ばれる少なくとも一種の酸又はそのアンモニウム塩であってもよく、また、それらの総含有量は1〜20質量%である。   Preferably, the electrolyte solution further contains another organic acid or an ammonium salt thereof such as boric acid or ammonium pentaborate, sebacic acid, azelaic acid, benzenecarboxylic acid, adipic acid, dodecanedioic acid, 1,6-dodecane. It may be at least one acid selected from diacids and 1,7-sebacic acid or an ammonium salt thereof, and the total content thereof is 1 to 20% by mass.

好ましく、前記電解液に、さらに、火花電圧を向上させることができる高分子化合物、例えば、ポリエチレングリコール、ポリビニルアルコール、ポリビニルアルコールボレート、ポリビニルアルコールホスフェート、ポリビニルピロリドンを含んでもよく、また、それらの総含有量は通常0.2〜15質量%、好ましくは0.5〜10質量%である。   Preferably, the electrolytic solution may further contain a polymer compound capable of improving a spark voltage, for example, polyethylene glycol, polyvinyl alcohol, polyvinyl alcohol borate, polyvinyl alcohol phosphate, polyvinyl pyrrolidone, and the total content thereof. The amount is usually 0.2 to 15% by mass, preferably 0.5 to 10% by mass.

好ましく、前記α位に分枝鎖を含有するジカルボン酸或いはその塩は、好ましくは主鎖がアジピン酸又はピメリン酸であり、すなわち、本発明にかかるα位に分枝鎖を含有するジカルボン酸がアジピン酸又はピメリン酸の誘導体である。α位に分枝鎖を含有するので、高温でエステル化とアミド化が発生しにくく、電解液電気伝導度の低下が遅くなり、その上、主鎖がアジピン酸又はピメリン酸であるため、エチレングリコールにおいての溶解性を大幅に向上することができる。   Preferably, the dicarboxylic acid or salt thereof containing a branched chain at the α-position is preferably adipic acid or pimelic acid as the main chain, that is, the dicarboxylic acid containing a branched chain at the α-position according to the present invention is It is a derivative of adipic acid or pimelic acid. Since it contains a branched chain at the α-position, esterification and amidation are less likely to occur at high temperatures, and the decrease in electrolyte electrical conductivity is slow, and in addition, the main chain is adipic acid or pimelic acid. The solubility in glycol can be greatly improved.

本発明の第2の目的は、次のような技術によって達成される。   The second object of the present invention is achieved by the following technique.

本発明にかかるα位に分枝鎖を含有するジカルボン酸が次のような化学式2(化2)(化学反応式(1),(2),(3))により製造されたものである。
(ここで、
R1は炭素数1〜20の炭化水素基または水素原子であり、この炭化水素基は、直鎖状又は分枝鎖状であってもよく、飽和又は不飽和であってもよい、また、主鎖又は分枝鎖には、エーテル基、エステル基、シアノ基、アミド基、ヒドロキシ基、カルボキシル基等を含んでもよく、好ましくは炭素数1〜8の炭化水素基または水素原子であり、
R2は炭素数1〜20の炭化水素基であり、この炭化水素基は、直鎖状又は分枝鎖状であってもよく、飽和又は不飽和であってもよい、また、主鎖及び分枝鎖には、エーテル基、エステル基、シアノ基、アミド基、ヒドロキシ基、カルボキシル基等を含んでもよく、好ましくは炭素数1〜8の炭化水素基であり、
R3、R4は同一又は異なっていてもよく炭素数1〜5の炭化水素基であり、好ましくは炭素数1〜2の炭化水素基であり、
Xは塩素、臭素、ヨウ素等のハロゲン原子又はスルホン基等であり、
nは2〜15の整数であり、好ましくは2〜3である。)
The dicarboxylic acid containing a branched chain at the α-position according to the present invention is produced by the following chemical formula 2 (Chemical formula 2) (chemical reaction formulas (1), (2), (3)).
(here,
R 1 is a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom, and this hydrocarbon group may be linear or branched, saturated or unsaturated, The main chain or branched chain may contain an ether group, an ester group, a cyano group, an amide group, a hydroxy group, a carboxyl group, etc., preferably a hydrocarbon group having 1 to 8 carbon atoms or a hydrogen atom,
R 2 is a hydrocarbon group having 1 to 20 carbon atoms, and this hydrocarbon group may be linear or branched, saturated or unsaturated, The branched chain may include an ether group, an ester group, a cyano group, an amide group, a hydroxy group, a carboxyl group, and the like, preferably a hydrocarbon group having 1 to 8 carbon atoms,
R 3 and R 4 may be the same or different and each represents a hydrocarbon group having 1 to 5 carbon atoms, preferably a hydrocarbon group having 1 to 2 carbon atoms,
X is a halogen atom such as chlorine, bromine, iodine, or a sulfone group;
n is an integer of 2 to 15, preferably 2 to 3. )

好ましく、前記α位に分枝鎖を含有するジカルボン酸が、次のようなステップで得られたものである。
(1)反応物Aと塩基を、反応物Aと塩基のモル比が0.8〜1.2:1となるように秤量し、反応溶媒に入れるステップと、
(2)30℃〜150℃の範囲から選ばれる温度で、1〜10時間の加熱反応を行うステップと、
(3)前記反応が終わった後、溶媒を蒸発させ、希酸で中性に中和するステップと、
(4)油層を取り分け、減圧蒸留により中間産物Bが得られるステップと、
(5)前記中間産物Bを溶媒に加え、等モルの塩基を加え、さらにR2Xを加えるステップと、
(6)60℃〜200℃の範囲から選ばれる温度で、2〜50時間の加熱反応を行うステップと、
(7)前記反応が終わった後、溶媒を蒸発させ、酸で中性に中和するステップと、
(8)油層を分離し、減圧蒸留により所望のエステルが得られるステップと、
(9)得られるエステルは、強塩基(KOH又はNaOH)により分解、酸性化、洗浄したあと、前記α位に分枝鎖を含有するジカルボン酸が得られるステップ。
Preferably, the dicarboxylic acid containing a branched chain at the α-position is obtained by the following steps.
(1) Weighing the reactant A and the base so that the molar ratio of the reactant A and the base is 0.8 to 1.2: 1 and putting it in the reaction solvent;
(2) performing a heating reaction for 1 to 10 hours at a temperature selected from the range of 30 ° C to 150 ° C;
(3) after the reaction is finished, evaporating the solvent and neutralizing with a dilute acid;
(4) separating the oil layer and obtaining intermediate product B by distillation under reduced pressure;
(5) adding the intermediate product B to a solvent, adding an equimolar base, and further adding R 2 X;
(6) performing a heating reaction for 2 to 50 hours at a temperature selected from the range of 60 ° C to 200 ° C;
(7) after the reaction is finished, evaporating the solvent and neutralizing with acid neutral;
(8) separating the oil layer and obtaining a desired ester by distillation under reduced pressure;
(9) The obtained ester is decomposed, acidified and washed with a strong base (KOH or NaOH) to obtain a dicarboxylic acid containing a branched chain at the α-position.

好ましく、アンモニウム塩を形成する必要があると、前記α位に分枝鎖を含有するジカルボン酸とアンモニア又はアミンを反応してα位に分枝鎖を含有するアンモニウム塩を形成することにより、電解液にエステル化或いはアミド化しにくくなるので、電解液に一層良い熱安定性を持たせる。   Preferably, when it is necessary to form an ammonium salt, the dicarboxylic acid containing a branched chain at the α-position is reacted with ammonia or an amine to form an ammonium salt containing a branched chain at the α-position. Since the solution is less likely to be esterified or amidated, the electrolyte solution has better thermal stability.

前記好ましい結果に基づいて、反応物Aはアジピン酸ジメチル(エチル)、ピメリン酸ジメチル(エチル)、2−メチル−アジピン酸ジメチル等であることが好ましい。   Based on the preferred result, the reactant A is preferably dimethyl (ethyl) adipate, dimethyl (ethyl) pimelate, dimethyl 2-methyl-adipate or the like.

前記好ましい結果として、本発明にかかるα位に分枝鎖を含有するジカルボン酸は、好ましくは、アジピン酸又はピメリン酸の誘導体、例えば、α−ヘキシルアジピン酸、α−ブチルアジピン酸、α−メチル−α’−ブチルアジピン酸、α−ヘキシルピメリン酸等である。   As a preferable result, the dicarboxylic acid containing a branched chain at the α-position according to the present invention is preferably adipic acid or a derivative of pimelic acid such as α-hexyladipic acid, α-butyladipic acid, α-methyl. -Α'-butyladipic acid, α-hexylpimelic acid and the like.

化学式2(化2)の化学反応式(1)と(2)に用いられる強塩基は、アルカリ金属或いはアルカリ土類金属のアルコキシド、アルカリ金属或いはアルカリ土類金属の水素化物、アルカリ金属或いはアルカリ土類金属の炭化水素基化合物、アルカリ金属或いはアルカリ土類金属のアンモニア又はアミン化合物から選ばれ、その中、化学反応式1において塩基と反応物Aの比例は、0.8〜1.2:1、好ましくは1.0〜1.10:1で、塩基がやや過量であり、化学反応式2において塩基と反応物Bのモル比は1:1である。前記二つの化学反応式において塩基は同一又は異なっていてもよく、前記塩基は、例えば、ナトリウムメトキシド、ナトリウムエトキシド、水素化ナトリウム、カリウムtert−ブトキシド、トリフェニルメタンナトリウム等が挙げられる。   The strong base used in the chemical reaction formulas (1) and (2) of Chemical Formula 2 (Chemical Formula 2) is alkali metal or alkaline earth metal alkoxide, alkali metal or alkaline earth metal hydride, alkali metal or alkaline earth. Selected from hydrocarbon group compounds of alkali metals, ammonia or amine compounds of alkali metals or alkaline earth metals, in which the ratio of base to reactant A in chemical reaction formula 1 is 0.8 to 1.2: 1, preferably 1.0. In ˜1.10: 1, the base is slightly overdose, and in the chemical reaction formula 2, the molar ratio of the base to the reactant B is 1: 1. In the two chemical reaction formulas, the bases may be the same or different, and examples of the base include sodium methoxide, sodium ethoxide, sodium hydride, potassium tert-butoxide, sodium triphenylmethane, and the like.

前記化学式2(化2)の化学反応式(1)と(2)の溶媒として、同一又は異なっていてもよく、アルコール系、エーテル系、アルコールエーテル系、アミド系、スルホン系、スルホキシド系などから選ばれ、好ましくは、メタノール、エタノール、tert−ブタノール、エチレングリコールジメチルエーテル、ジエチレングリコールジメチルエーテル、テトラヒドロフラン等である。   The solvents of the chemical reaction formulas (1) and (2) of the chemical formula 2 (Chemical Formula 2) may be the same or different, and are alcohol-based, ether-based, alcohol ether-based, amide-based, sulfone-based, sulfoxide-based and the like. Preferred are methanol, ethanol, tert-butanol, ethylene glycol dimethyl ether, diethylene glycol dimethyl ether, tetrahydrofuran and the like.

R2XとBの反応モル比が理論的に1:1、好ましくは0.8〜1.2:1、より好ましくは1.0〜1.1:1で、R2Xは等量又はやや過量である。 The reaction molar ratio of R 2 X and B is theoretically 1: 1, preferably 0.8 to 1.2: 1, more preferably 1.0 to 1.1: 1, and R 2 X is equivalent or slightly overdose.

化学式2(化2)の化学反応式(1)の反応温度は30℃〜150℃の範囲から選ばれ、好ましくは、40〜80℃であり、反応時間は1〜10時間、好ましくは2〜7時間である。   The reaction temperature of the chemical reaction formula (1) of the chemical formula 2 (Chemical Formula 2) is selected from the range of 30 ° C. to 150 ° C., preferably 40 ° C. to 80 ° C., and the reaction time is 1 to 10 hours, preferably 2 to 7 hours.

化学式2(化2)の化学反応式(2)の反応温度は60℃〜200℃の範囲から選ばれ、好ましくは、70〜150℃であり、反応時間は2〜50時間、好ましくは5〜30時間である。   The reaction temperature of the chemical reaction formula (2) of the chemical formula 2 (Chemical Formula 2) is selected from the range of 60 ° C. to 200 ° C., preferably 70 to 150 ° C., and the reaction time is 2 to 50 hours, preferably 5 to 30 hours.

反応物Aは強塩基と溶媒との反応が終わった後、反応液を酸で中性に中和し、油層を取り分け、減圧蒸留により中間産物Bが得られる。そして、中間産物Bを溶媒と強塩基に加え、更にR2Xと反応させ、反応液を酸で中性に中和し、油層を取り分け、減圧蒸留によりエステルが得られる。濃NaOH又はKOHによりそのエステルが酸性型に分解され、酸性化した後で洗浄し、本発明にかかるα位に分枝鎖を含有するジカルボン酸が得られる。そのジカルボン酸をアンモニア又はアミンと反応してアンモニウム塩を形成する。そのジカルボン酸或いは塩は、本発明にかかる中高圧溶質になる。 After the reaction of the reactant A with the strong base and the solvent is completed, the reaction solution is neutralized with an acid and the oil layer is separated, and an intermediate product B is obtained by distillation under reduced pressure. Then, the intermediate product B is added to a solvent and a strong base, and further reacted with R 2 X. The reaction solution is neutralized with an acid, an oil layer is separated, and an ester is obtained by distillation under reduced pressure. The ester is decomposed into an acidic form by concentrated NaOH or KOH, and after acidification, it is washed to obtain a dicarboxylic acid containing a branched chain at the α-position according to the present invention. The dicarboxylic acid is reacted with ammonia or an amine to form an ammonium salt. The dicarboxylic acid or salt becomes a medium-high pressure solute according to the present invention.

本発明に基づいて提供する技術手段は、従来の技術と比べると、次のような幾つかの利点がある。   The technical means provided based on the present invention has several advantages over the prior art.

本発明にかかるα位に分枝鎖を含有するジカルボン酸或いはその塩から得られた電解液は、エチレングリコールにおいて、一層良い溶解性と熱安定性を有する。   An electrolytic solution obtained from a dicarboxylic acid containing a branched chain at the α-position or a salt thereof according to the present invention has better solubility and thermal stability in ethylene glycol.

当該電解液を含有する中高圧アルミニウム電解コンデンサは、寿命が長く、低温性能に優れている利点がある。発明を実施する形態において、本発明の具体的な効果を詳しく説明して分析する。   The medium-high pressure aluminum electrolytic capacitor containing the electrolytic solution has an advantage of having a long life and excellent low-temperature performance. In the embodiments of the present invention, specific effects of the present invention will be described in detail and analyzed.

以下、本発明の内容をさらに説明するために、具体的な実施例に基づいて、本発明を詳細に説明する。   Hereinafter, in order to further explain the contents of the present invention, the present invention will be described in detail based on specific examples.

実施例1
アジピン酸ジエチル70g(0.4mol)を500ml三つ口フラスコに仕込み、ジエチレングリコールジメチルエーテル210gを加え、攪拌しながらナトリウムメトキシド23g(0.43mol)を加え、50℃に加熱して3時間減圧反応させ、反応が終わった後、溶媒を蒸発させた。残り物をH2SO4で中性に中和し、油層を取り分け、減圧蒸留により中間産物B 40gが得られ、その中間産物Bを500ml三つ口フラスコに仕込み、ナトリウムメトキシド15.2gを加え、さらに、tert−ブタノール140gを加え、還流下で(80-85℃)ブロモヘキサン49gを滴下して24時間反応させた。反応が終わった後、tert−ブタノールを蒸発させ、H2SO4で中性に中和し、油層を取り分けて減圧蒸留し、加熱で濃NaOH溶液を使用して酸性型に分解させた。H2SO4で中和した後で洗浄し、乾燥して2−へキシルアジピン酸47gが得られた。総収率は約51%である。
Example 1
Diethyl adipate 70 g (0.4 mol) was charged into a 500 ml three-necked flask, 210 g of diethylene glycol dimethyl ether was added, and 23 g (0.43 mol) of sodium methoxide was added with stirring. After the end of the solvent was evaporated. The residue was neutralized with H 2 SO 4 and the oil layer was separated, and 40 g of intermediate product B was obtained by distillation under reduced pressure. Further, 140 g of tert-butanol was added, and 49 g of bromohexane was added dropwise under reflux (80-85 ° C.) to react for 24 hours. After the reaction was completed, tert- butanol was evaporated, neutralized neutralized with H 2 SO 4, and especially the oil layer was distilled under reduced pressure using concentrated NaOH solution to decompose the acid form by heating. After neutralizing with H 2 SO 4 , washing and drying were performed to obtain 47 g of 2-hexyladipic acid. The total yield is about 51%.

実施例2
アジピン酸ジエチル70g(0.4mol)を500ml三つ口フラスコに仕込み、ジエチレングリコールジメチルエーテル210gを加え、攪拌しながらナトリウムメトキシド23g(0.43mol)を加え、50℃に加熱して3時間減圧反応させ、反応が終わった後、溶媒を蒸発させた。残り物をH2SO4で中性に中和し、油層を取り分け、減圧蒸留により中間産物B 41gが得られ、その中間産物Bを500ml三つ口フラスコに仕込み、ギ酸ナトリウム15.6gを加え、さらに、tert−ブタノール140gを加え、還流下で(80-85℃)ブロモブタン42gを滴下して24時間反応させた。反応が終わった後、tert−ブタノールを留去し、H2SO4で中性に中和した。油層を取り分けて減圧蒸留し、加熱で濃NaOH溶液を使用して酸性型に分解させた。H2SO4で中和した後で洗浄し、乾燥して2−ブチルアジピン酸37gが得られた。収率は約46%である。
得られた酸をアンモニアと反応させ、アンモニウム塩になり、エチレングリコール溶液に調製して電解液とする。その効果を説明するために、従来のセバシン酸アンモニウムのエチレングリコール溶液と比べた結果を表1に示す。
Example 2
Diethyl adipate 70 g (0.4 mol) was charged into a 500 ml three-necked flask, 210 g of diethylene glycol dimethyl ether was added, and 23 g (0.43 mol) of sodium methoxide was added with stirring. After the end of the solvent was evaporated. The residue is neutralized with H 2 SO 4 and the oil layer is separated, and 41 g of intermediate product B is obtained by distillation under reduced pressure. , 140 g of tert-butanol was added, and 42 g of bromobutane was added dropwise under reflux (80-85 ° C.) to react for 24 hours. After the reaction was completed, tert-butanol was distilled off, and neutralized with H 2 SO 4 . The oil layer was separated, distilled under reduced pressure, and decomposed to the acidic form using concentrated NaOH solution by heating. After neutralizing with H 2 SO 4 , washing and drying were performed to obtain 37 g of 2-butyladipic acid. The yield is about 46%.
The obtained acid is reacted with ammonia to form an ammonium salt, which is prepared into an ethylene glycol solution to obtain an electrolytic solution. In order to explain the effect, Table 1 shows the results compared with a conventional ethylene glycol solution of ammonium sebacate.

実施例3
実施例1で得られた酸のアンモニウム塩を作成して、5%エチレングリコール溶液250gを調製し、さらに、0.1%次亜燐酸アンモニウム、0.4% p−ニトロベンジルアルコールを加えて電解液を作成した。得られた電解液を500mlステンレス瓶に仕込み、密封、105℃で恒温して各パラメーターを測定した。その結果を表2に示す。
Example 3
An ammonium salt of the acid obtained in Example 1 was prepared to prepare 250 g of a 5% ethylene glycol solution, and 0.1% ammonium hypophosphite and 0.4% p-nitrobenzyl alcohol were further added to prepare an electrolytic solution. . The obtained electrolyte solution was charged into a 500 ml stainless steel bottle, sealed, and kept at 105 ° C. to measure each parameter. The results are shown in Table 2.

比較例1
5%セバシン酸アンモニウムエチレングリコール溶液250gに、0.1%次亜燐酸アンモニウム、0.4% p−ニトロベンジルアルコールを加えてを加え、500mlステンレス瓶に仕込み、密封、105℃で恒温して測定した。その結果を表2に示す。
Comparative Example 1
To 250 g of 5% ammonium sebacate ethylene glycol solution, 0.1% ammonium hypophosphite and 0.4% p-nitrobenzyl alcohol were added, and the mixture was placed in a 500 ml stainless steel bottle, sealed, and kept at 105 ° C. for measurement. The results are shown in Table 2.

表1と表2のデータを分析した結果を次に示す。   The results of analyzing the data in Tables 1 and 2 are as follows.

実施例1で得られた酸のアンモニウム塩は室温下で20%エチレングリコール溶液に調製することができ、かつ、透明な溶液が得られる。それに対して、セバシン酸アンモニウムは10%エチレングリコール溶液に調製すると、室温下で溶質が析出したので、本発明にかかる溶質はエチレングリコール溶液において一層良い溶解性を有する。   The ammonium salt of the acid obtained in Example 1 can be prepared in a 20% ethylene glycol solution at room temperature and a clear solution is obtained. In contrast, when ammonium sebacate was prepared in a 10% ethylene glycol solution, the solute precipitated at room temperature, so the solute according to the present invention has better solubility in the ethylene glycol solution.

実施例3で得られた電解液の導電率初期値は、30℃で1610μS/cmであるが、比較例1の電解液の導電率は、30℃で2010μS/cmであるので、初期値は比較例1電解液のほうが高いである。105℃、500時間恒温した後、実施例3電解液の導電率は、30℃で1040μS/cmになるように35%低下したが、比較例1は同じ場合、690μS/cmになるように66%低下した。105℃、1172時間を経て、実施例3の電解液は、30℃での導電率が921μS/cmになるように43%低下したが、比較例1は同じ条件において、598μS/cmになるように70%低下した。セバシン酸アンモニウムの5%エチレングリコール溶液に基づく電解液と比べて、本発明にかかる酸のアンモニウム塩の5%エチレングリコール溶液に基づく電解液は、導電率の低下が相対的に遅いである。セバシン酸アンモニウムに基づく電解液は、導電率の初期値がもっと高いといっても、恒温した後、本発明にかかる酸のアンモニウム塩に基づく電解液は、導電率が一層高いである。以上のことから、本発明にかかる酸及びそのアンモニウム塩から得られた電解液が一層良い熱安定性があることが分かる。   The initial conductivity value of the electrolytic solution obtained in Example 3 is 1610 μS / cm at 30 ° C., but since the electrical conductivity of the electrolytic solution of Comparative Example 1 is 2010 μS / cm at 30 ° C., the initial value is Comparative Example 1 The electrolytic solution is higher. After constant temperature at 105 ° C. for 500 hours, the conductivity of Example 3 electrolyte was reduced by 35% to be 1040 μS / cm at 30 ° C., but Comparative Example 1 was the same so that it was 690 μS / cm. % Decreased. After 105 ° C. and 1172 hours, the electrolyte of Example 3 decreased by 43% so that the conductivity at 30 ° C. was 921 μS / cm, but Comparative Example 1 was 598 μS / cm under the same conditions. Decreased by 70%. Compared with an electrolytic solution based on a 5% ethylene glycol solution of ammonium sebacate, the electrolytic solution based on a 5% ethylene glycol solution of an ammonium salt of an acid according to the present invention has a relatively slow decrease in conductivity. Even though the electrolyte based on ammonium sebacate has a higher initial value of conductivity, the electrolyte based on the ammonium salt of the acid according to the present invention has a higher conductivity after the temperature is maintained. From the above, it can be seen that the electrolytic solution obtained from the acid according to the present invention and its ammonium salt has better thermal stability.

前述の実施例は、本発明を実施するための最良の形態であり、本発明はこれらの実施例のみに限定されるものではない。要するに本発明の主旨を損なわずになされた種々の変形は、依然として本発明の技術的範囲に属するものである。
The foregoing embodiments are the best modes for carrying out the present invention, and the present invention is not limited to these embodiments. In short, various modifications made without impairing the gist of the present invention still belong to the technical scope of the present invention.

Claims (3)

α位に分枝鎖を含有するジカルボン酸の製造方法であって、
前記α位に分枝鎖を含有するジカルボン酸が、次のような化学式3(化3)で表され、
(上式中、
R1は炭素数1〜20の炭化水素基または水素原子であり、
R2は炭素数1〜20の炭化水素基であり、
nは2〜15の整数である。)
かつ、
下記の化学式4(化4)の三つの反応を含む
(ここで、
R1は炭素数1〜20の炭化水素基または水素原子であり、
R2は炭素数1〜20の炭化水素基であり、
R3、R4は炭素数1〜5の炭化水素基であり、
Xは塩素、臭素、ヨウ素又はスルホン基であり、
nは2〜15の整数である。)
ことを特徴とするα位に分枝鎖を含有するジカルボン酸の製造方法。
A method for producing a dicarboxylic acid containing a branched chain at the α-position,
The dicarboxylic acid containing a branched chain at the α-position is represented by the following chemical formula 3 (Chemical Formula 3):
(In the above formula,
R 1 is a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom,
R 2 is a hydrocarbon group having 1 to 20 carbon atoms,
n is an integer of 2-15. )
And,
Including three reactions of the following chemical formula 4
(here,
R 1 is a hydrocarbon group having 1 to 20 carbon atoms or a hydrogen atom,
R 2 is a hydrocarbon group having 1 to 20 carbon atoms,
R 3 and R 4 are hydrocarbon groups having 1 to 5 carbon atoms,
X is a chlorine, bromine, iodine or sulfone group,
n is an integer of 2-15. )
A process for producing a dicarboxylic acid containing a branched chain at the α-position.
(1)反応物Aと塩基を、反応物Aと塩基のモル比が0.8〜1.2:1となるように秤量し、反応溶媒に入れるステップと、
(2)30℃〜150℃の範囲から選ばれる温度で、1〜10時間の加熱反応を行うステップと、
(3)前記反応が終わった後、溶媒を蒸発させ、希酸で中性に中和するステップと、
(4)油層を取り分け、減圧蒸留により中間産物Bが得られるステップと、
(5)前記中間産物Bを溶媒に加え、等モルの塩基を加え、さらにR2Xを加えるステップと、
(6)60℃〜200℃の範囲から選ばれる温度で、2〜50時間の加熱反応を行うステップと、
(7)前記反応が終わった後、溶媒を蒸発させ、酸で中性に中和するステップと、
(8)油層を分離し、減圧蒸留によりエステル系化合物が得られるステップと、
(9)得られるエステル系化合物は、強塩基により分解、酸性化、洗浄したあと、前記α位に分枝鎖を含有するジカルボン酸が得られるステップと、
を有する製造方法により、前記α位に分枝鎖を含有するジカルボン酸を製造する、
ことを特徴とする請求項1記載のα位に分枝鎖を含有するジカルボン酸の製造方法。
(1) Weighing the reactant A and the base so that the molar ratio of the reactant A and the base is 0.8 to 1.2: 1 and putting it in the reaction solvent;
(2) performing a heating reaction for 1 to 10 hours at a temperature selected from the range of 30 ° C to 150 ° C;
(3) after the reaction is finished, evaporating the solvent and neutralizing with a dilute acid;
(4) separating the oil layer and obtaining intermediate product B by distillation under reduced pressure;
(5) adding the intermediate product B to a solvent, adding an equimolar base, and further adding R 2 X;
(6) performing a heating reaction for 2 to 50 hours at a temperature selected from the range of 60 ° C to 200 ° C;
(7) after the reaction is finished, evaporating the solvent and neutralizing with acid neutral;
(8) separating the oil layer and obtaining an ester compound by distillation under reduced pressure;
(9) The obtained ester compound is decomposed, acidified and washed with a strong base, and then a dicarboxylic acid containing a branched chain at the α-position is obtained;
A dicarboxylic acid containing a branched chain at the α-position is produced by a production method comprising:
The method for producing a dicarboxylic acid containing a branched chain at the α-position according to claim 1.
前記α位に分枝鎖を含有するジカルボン酸の塩とは、α位に分枝鎖を含有するジカルボン酸とアンモニア又はアミンから形成する塩である、
ことを特徴とする請求項1又は2記載のアルミニウム電解コンデンサ電解液。
The salt of a dicarboxylic acid containing a branched chain at the α-position is a salt formed from a dicarboxylic acid containing a branched chain at the α-position and ammonia or an amine.
The aluminum electrolytic capacitor electrolyte according to claim 1 or 2, wherein
JP2012070588A 2009-03-27 2012-03-27 Aluminum electrolytic capacitor electrolyte and method for producing core solute thereof Active JP5466256B2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN200910106241.3 2009-03-27
CN2009101062413A CN101521117B (en) 2009-03-27 2009-03-27 preparation method of alpha- dicarboxylic acids for electrolyte for aluminium electrolytic capacitor

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP2009214020A Division JP2010232630A (en) 2009-03-27 2009-09-16 Aluminum electrolytic capacitor electrolyte, and method of manufacturing core solute thereof

Publications (2)

Publication Number Publication Date
JP2012134550A true JP2012134550A (en) 2012-07-12
JP5466256B2 JP5466256B2 (en) 2014-04-09

Family

ID=41081646

Family Applications (2)

Application Number Title Priority Date Filing Date
JP2009214020A Pending JP2010232630A (en) 2009-03-27 2009-09-16 Aluminum electrolytic capacitor electrolyte, and method of manufacturing core solute thereof
JP2012070588A Active JP5466256B2 (en) 2009-03-27 2012-03-27 Aluminum electrolytic capacitor electrolyte and method for producing core solute thereof

Family Applications Before (1)

Application Number Title Priority Date Filing Date
JP2009214020A Pending JP2010232630A (en) 2009-03-27 2009-09-16 Aluminum electrolytic capacitor electrolyte, and method of manufacturing core solute thereof

Country Status (2)

Country Link
JP (2) JP2010232630A (en)
CN (1) CN101521117B (en)

Families Citing this family (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102074367B (en) * 2010-12-24 2013-04-24 东莞宏强电子有限公司 Preparation method for novel high molecular weight branched chain diacid electrolyte, product and application thereof
CN102842430B (en) * 2012-08-06 2017-05-17 深圳新宙邦科技股份有限公司 Aluminum electrolytic capacitor electrolyte and aluminum electrolytic capacitor
CN103632851B (en) * 2012-08-27 2016-08-17 深圳市金元电子技术有限公司 High conductivity boron series-free working electrolyte and preparation method thereof
CN103632850B (en) * 2012-08-27 2016-08-17 深圳市金元电子技术有限公司 High flash over voltage boron series-free working electrolyte and preparation method thereof
CN102969161B (en) * 2012-12-18 2016-01-20 南通新三能电子有限公司 The preparation method of aluminium electrolytic capacitor driving electrolytic solution and main solute thereof
CN102983007A (en) * 2012-12-25 2013-03-20 上海赛特康新能源科技有限公司 Novel nano aluminum electrolytic capacitor
CN103086871B (en) * 2013-02-02 2014-12-10 刘珍明 Preparation method of dicarboxylic acid with branch at alpha position for aluminum electrolytic capacitor electrolyte
JP6201172B2 (en) * 2013-08-05 2017-09-27 国立大学法人三重大学 Electrolytic capacitor driving electrolyte and electrolytic capacitor using the same
CN103700506B (en) * 2013-12-25 2016-06-29 佛山市高明区利明电子有限公司 A kind of 160V electrolysis condenser and production technology thereof
CN103928234A (en) * 2014-04-28 2014-07-16 南通瑞泰电子有限公司 Electrolyte for aluminum electrolytic capacitor
CN104282439A (en) * 2014-10-29 2015-01-14 福建云星电子有限公司 Boric-acid-system-free electrolyte and preparation method thereof
CN107845504B (en) * 2016-09-19 2020-07-24 深圳新宙邦科技股份有限公司 Electrolyte for aluminum electrolytic capacitor and aluminum electrolytic capacitor using the same
JP6399466B2 (en) * 2017-02-01 2018-10-03 国立大学法人三重大学 Electrolytic capacitor driving electrolyte and electrolytic capacitor using the same
CN109192513B (en) * 2018-09-05 2020-10-09 武汉海斯普林科技发展有限公司 Process for preparing ammonium salt mixtures of branched polycarboxylic acids
CN109180472B (en) * 2018-09-20 2021-03-19 武汉海斯普林科技发展有限公司 Preparation method of 2-hexyl adipic acid
CN109741946A (en) * 2019-01-25 2019-05-10 南通瑞泰电子有限公司 A kind of preparation method and application of the main solute of high-performance aluminum electrolyte for electrolytic capacitor
CN110687019B (en) * 2019-10-30 2020-09-08 华中科技大学 Device and method for electrochemical hydrogen permeation measurement in high-temperature environment
CN110718391A (en) * 2019-11-18 2020-01-21 益阳市华琳电子有限公司 Electrolyte for aluminum electrolytic capacitor and preparation method thereof
CN112028741B (en) * 2020-09-27 2021-06-08 上海交通大学 Electrolyte for ultrahigh-voltage aluminum electrolytic capacitor and preparation method and application thereof
TWI766400B (en) * 2020-10-23 2022-06-01 財團法人工業技術研究院 Electrolyte and compound for the electrolyte and capacitor

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02298007A (en) * 1989-05-12 1990-12-10 Matsushita Electric Ind Co Ltd Electrolyte for electrolytic capacitor drive use
JPH06275472A (en) * 1993-03-19 1994-09-30 Matsushita Electric Ind Co Ltd Electrolyte for driving electrolytic capacitor and electrolytic capacitor using same
JPH0982577A (en) * 1995-09-11 1997-03-28 Hitachi Aic Inc Electrolyte for electrolytic capacitor
JPH1167605A (en) * 1997-08-08 1999-03-09 Nippon Chemicon Corp Electrolytic solution for electrolytic capacitor
JP2000091158A (en) * 1998-07-17 2000-03-31 Nippon Chemicon Corp Electrolyte for electrolytic capacitor
JP2003163139A (en) * 2001-11-26 2003-06-06 Daicel Chem Ind Ltd Electrolyte for electrolytic capacitor
WO2003050828A1 (en) * 2001-12-11 2003-06-19 Okamura Oil Mill. Ltd. Composition for electrolytic solution and process for producing the same
JP2004047595A (en) * 2002-07-10 2004-02-12 Sanyo Chem Ind Ltd Electrolyte
JP2006229176A (en) * 2004-02-26 2006-08-31 Sanyo Chem Ind Ltd Electrolyte

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101004976B (en) * 2007-01-09 2010-05-19 东莞市东阳光电容器有限公司 Electrolyte of electrolytic capacitor

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02298007A (en) * 1989-05-12 1990-12-10 Matsushita Electric Ind Co Ltd Electrolyte for electrolytic capacitor drive use
JPH06275472A (en) * 1993-03-19 1994-09-30 Matsushita Electric Ind Co Ltd Electrolyte for driving electrolytic capacitor and electrolytic capacitor using same
JPH0982577A (en) * 1995-09-11 1997-03-28 Hitachi Aic Inc Electrolyte for electrolytic capacitor
JPH1167605A (en) * 1997-08-08 1999-03-09 Nippon Chemicon Corp Electrolytic solution for electrolytic capacitor
JP2000091158A (en) * 1998-07-17 2000-03-31 Nippon Chemicon Corp Electrolyte for electrolytic capacitor
JP2003163139A (en) * 2001-11-26 2003-06-06 Daicel Chem Ind Ltd Electrolyte for electrolytic capacitor
WO2003050828A1 (en) * 2001-12-11 2003-06-19 Okamura Oil Mill. Ltd. Composition for electrolytic solution and process for producing the same
JP2004047595A (en) * 2002-07-10 2004-02-12 Sanyo Chem Ind Ltd Electrolyte
JP2006229176A (en) * 2004-02-26 2006-08-31 Sanyo Chem Ind Ltd Electrolyte

Also Published As

Publication number Publication date
JP2010232630A (en) 2010-10-14
CN101521117A (en) 2009-09-02
JP5466256B2 (en) 2014-04-09
CN101521117B (en) 2011-06-29

Similar Documents

Publication Publication Date Title
JP5466256B2 (en) Aluminum electrolytic capacitor electrolyte and method for producing core solute thereof
JP4860720B2 (en) Electrolytic solution for aluminum electrolytic capacitor and method for producing solute thereof
CN101206955B (en) Branched chain polybasic carboxylic acid ammonium salt mixture as well as preparation method and application thereof
JP2009249379A (en) Ionic liquid miscible with various polar/nonpolar solvent and method for producing the same
JP6530167B2 (en) Carbon dioxide chemical absorption liquid and carbon dioxide separation and recovery method
CN109741946A (en) A kind of preparation method and application of the main solute of high-performance aluminum electrolyte for electrolytic capacitor
JP2016134406A (en) Carboxylic acid compound useful as solute for electrolyte for power storage device and method for producing the same
JP5014854B2 (en) Aminosiloxane ionic liquid
JP2007126611A (en) Long chain dibasic acid
US8345407B2 (en) Low viscosity ionic liquids
KR100922706B1 (en) Composition for electrolytic solution and process for producing the same
JP2010171087A (en) Electrolyte composition, production process thereof, and electrolyte for driving aluminum electrolytic capacitor containing electrolyte composition
JP4787558B2 (en) Long chain polybasic acid mixture
JP2005104846A (en) Quaternary ammonium ambient-temperature molten salt and its manufacturing method
JP6445979B2 (en) Charge transport material for photoelectrochemical devices
KR102446846B1 (en) Fluoride alkyl glycerin derivatives, preparation method therefor and use thereof
CN109192513B (en) Process for preparing ammonium salt mixtures of branched polycarboxylic acids
KR101162713B1 (en) A Preparation Method For High Pure Ionic Liquid
TWI672291B (en) Electrolyte capacitor and electrolytic capacitor
JP2009196925A (en) Organic salt
JP2001057320A (en) Electrolyte for electrolytic capacitor
Liu et al. Polyether-based ionic liquids from simple mixing of terminal diamines with organic acids to dicationic diammonium carboxylates
JP2004349525A (en) Conductive polymer and solid-state electrolytic capacitor using same
WO2024194599A1 (en) Ionic liquids
JP2017055060A (en) Electrolytic solution for electrolytic capacitor

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20130716

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20130723

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20130925

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20140107

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20140123

R150 Certificate of patent or registration of utility model

Ref document number: 5466256

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250