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JPH0826053B2 - Method for producing quaternary phosphonium inorganic acid salt - Google Patents
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JPH0826053B2 - Method for producing quaternary phosphonium inorganic acid salt - Google Patents

Method for producing quaternary phosphonium inorganic acid salt

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Publication number
JPH0826053B2
JPH0826053B2 JP12542887A JP12542887A JPH0826053B2 JP H0826053 B2 JPH0826053 B2 JP H0826053B2 JP 12542887 A JP12542887 A JP 12542887A JP 12542887 A JP12542887 A JP 12542887A JP H0826053 B2 JPH0826053 B2 JP H0826053B2
Authority
JP
Japan
Prior art keywords
quaternary phosphonium
inorganic acid
reaction
carbonate
acid salt
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.)
Expired - Fee Related
Application number
JP12542887A
Other languages
Japanese (ja)
Other versions
JPS63290890A (en
Inventor
彰一郎 森
和彦 井田
誠 宇恵
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 Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP12542887A priority Critical patent/JPH0826053B2/en
Priority to US07/192,524 priority patent/US4892944A/en
Priority to EP88107735A priority patent/EP0291074B1/en
Priority to DE8888107735T priority patent/DE3868138D1/en
Publication of JPS63290890A publication Critical patent/JPS63290890A/en
Publication of JPH0826053B2 publication Critical patent/JPH0826053B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ホスフィン類を炭酸ジエステルと反応させ
ることにより、対応する四級ホスホニウム炭酸塩とし、
さらにこれに無機酸を混合して脱炭酸することにより、
四級ホスホニウム無機酸塩を製造する方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention provides a corresponding quaternary phosphonium carbonate by reacting a phosphine with a carbonic acid diester,
By further mixing this with an inorganic acid and decarboxylation,
It relates to a method for producing a quaternary phosphonium inorganic acid salt.

本発明の方法で得られる四級ホスホニウム無機酸塩
は、相関移動触媒などの各種触媒、水系及び有機系の電
解液のための電解質、各種の添加物、薬品として幅広い
分野で使用される有用な有機化合物である。
The quaternary phosphonium inorganic acid salt obtained by the method of the present invention is useful in various fields such as various catalysts such as phase transfer catalysts, electrolytes for aqueous and organic electrolytic solutions, various additives, and chemicals. It is an organic compound.

〔従来の技術〕[Conventional technology]

四級ホスホニウム塩の合成方法としては一般にホスフ
ィン類をアルキルハライド、ジアルキル硫酸などで加熱
下で四級化する方法が採用されている。又、陰イオン種
を種々に変化させた四級ホスホニウム塩を製造する場合
には、通常四級ホスホニウムハライド(塩化物、臭化
物、ヨウ化物)の陰イオン交換による方法が採用されて
いる。例えば、下記に示すような反応式に従って、四級
アンモニウム臭化物を四級ホスホニウム水酸化物に転換
したのち(反応1a)無機酸によって中和処理する方法
(反応1b)、四級ホスホニウム臭化物を無機酸と反応さ
せ、対応する無機酸塩が不溶な溶媒を選定することによ
り析出分離する方法(反応2)、四級ホスホニウム臭化
物と無機酸のアルカリ金属塩とを反応させ、無機酸塩を
析出または抽出により得る方法(反応3)、さらには四
級ホスホニウム臭化物と無機酸の銀塩を反応させて臭化
銀を析出させて液から目的物を得る方法(反応4)な
どを例示することができる。
As a method of synthesizing a quaternary phosphonium salt, a method of quaternizing a phosphine with an alkyl halide, a dialkyl sulfuric acid or the like under heating is generally adopted. Further, in the case of producing a quaternary phosphonium salt in which anion species are variously changed, a method of anion exchange of a quaternary phosphonium halide (chloride, bromide, iodide) is usually adopted. For example, according to the reaction formula shown below, a method of converting a quaternary ammonium bromide into a quaternary phosphonium hydroxide (reaction 1a) and then neutralizing the quaternary phosphonium bromide with an inorganic acid (reaction 1b). By reacting with a corresponding inorganic acid salt and selecting a solvent in which the corresponding inorganic acid salt is insoluble (reaction 2), and reacting a quaternary phosphonium bromide with an alkali metal salt of an inorganic acid to precipitate or extract the inorganic acid salt. The method (reaction 3), and the method of reacting a quaternary phosphonium bromide with a silver salt of an inorganic acid to precipitate silver bromide to obtain the desired product from the solution (reaction 4) can be exemplified.

R4 Br →R4 OH (反応1a) R4 OH +H →R4 +H2O (反応1b) R4 Br +H →R4 ↓+HBr (反応2) R4 Br +Na →R4 +NaBr (反応3) R4 Br +Ag →R4 +AgBr↓(反応4) 反応1aによる四級ホスホニウム水酸化物の製造法とし
ては、適当な溶媒に溶かした四級ホスホニウム臭化物を
四級ホスホニウム水酸化物型のイオン交換樹脂と反応さ
せる方法、四級ホスホニウム臭化物を液状媒体中でアル
カリ金属水酸化物と反応させる方法、電気化学的方法に
より臭素イオンをBr2として分離し、水酸化物を得る方
法、さらには銀化合物を用いる方法などが知られてい
る。
RFourP Br → RFourP OH  (Reaction 1a) RFourP OH + H A → RFourP A + H2O (Reaction 1b) RFourP Br + H A → RFourP A ↓ + HBr (Reaction 2) RFourP Br + Na A → RFourP A + NaBr (Reaction 3) RFourP Br + Ag A → RFourP A + AgBr ↓ (Reaction 4) As a method for producing quaternary phosphonium hydroxide by reaction 1a
Quaternary phosphonium bromide dissolved in a suitable solvent
Reacts with quaternary phosphonium hydroxide type ion exchange resins
The quaternary phosphonium bromide in a liquid medium.
For reaction with potassium metal hydroxide, electrochemical method
Br bromine ion2To obtain hydroxide by separating as
Methods, and methods using silver compounds are known.
It

〔発明が解決しようとする問題点〕[Problems to be solved by the invention]

しかしながら、反応1aによるいずれの方法も四級ホス
ホニウム水酸化物の製法とし高価な方法であり、又一般
に四級ホスホニウム水酸化物中の臭素イオンを完全に除
くことは困難であるので、反応1bによる中和生成物の純
度に問題を生ずることが多い。また、反応2および3の
方法においては、目的とする四級ホスホニウム無機酸塩
中の臭素イオンの除去はかなり困難であり、高純度の四
級ホスホニウム無機酸塩を得る製造法としては不適当で
ある。反応4に基づく方法は定量的な反応を行わせる方
法としては好ましいものと考えられるが、原料となる無
機酸の銀塩がきわめて高価であり、工業的に採用できる
方法とは言い難い。
However, any method according to Reaction 1a is an expensive method as a method for producing a quaternary phosphonium hydroxide, and it is generally difficult to completely remove the bromine ion in the quaternary phosphonium hydroxide, so that according to Reaction 1b Problems often occur in the purity of the neutralized product. Further, in the methods of Reactions 2 and 3, it is quite difficult to remove the bromine ion in the intended quaternary phosphonium inorganic acid salt, and it is unsuitable as a production method for obtaining a high-purity quaternary phosphonium inorganic acid salt. is there. The method based on reaction 4 is considered to be preferable as a method for carrying out a quantitative reaction, but the silver salt of an inorganic acid as a raw material is extremely expensive, and it is hard to say that it can be industrially adopted.

以上、四級ホスホニウム臭化物を一例として述べた
が、他のハライド、硫酸塩などを用いた場合も同様であ
り、一般に効率的かつ高純度で種々の陰イオン交換した
塩を作る方法は知られていない。
Although the quaternary phosphonium bromide has been described above as an example, the same is true when other halides, sulfates, etc. are used, and generally, a method for producing various anion-exchanged salts with high efficiency and high purity is known. Absent.

〔問題点を解決するための手段〕[Means for solving problems]

本発明者らは、従来の方法に較べて効率的な生産が可
能となり、かつ目的生成物の純度を高める工業的製法に
関する新しい技術を確立し、本発明に到達したものであ
る。
The present inventors have reached the present invention by establishing a new technique relating to an industrial production method that enables efficient production as compared with the conventional method and enhances the purity of the target product.

すなわち、本発明は、四級ホスホニウムの無機酸塩を
製造する方法において、 (a)ホスフィン類を炭酸ジエステルと反応させること
により、対応する四級ホスホニウム炭酸塩を製造する工
程 (b)さらに、生成してくる四級ホスホニウム炭酸塩を
無機酸と混合して炭酸ガスを系外に除去せしめて対応す
る無機酸塩を製造する工程の2段階の工程を経ることを
特徴とする四級ホスホニウム無機酸塩の製造方法を提案
するものである。
That is, the present invention relates to a method for producing a quaternary phosphonium inorganic acid salt, comprising the steps of: (a) reacting a phosphine with a carbonic acid diester to produce a corresponding quaternary phosphonium carbonate (b). A quaternary phosphonium inorganic acid characterized by being subjected to a two-step process of mixing the incoming quaternary phosphonium carbonate with an inorganic acid to remove carbon dioxide gas outside the system to produce a corresponding inorganic acid salt. It proposes a salt production method.

〔発明の具体的説明〕[Specific Description of the Invention]

本発明の原料となるホスフィン類としては、トリメチ
ルホスフィン、ジエチルメチルホスフィン、トリエチル
ホスフィン、トリ−n−プロピルホスフィン、トリ−n
−ブチルホスフィン、トリ−n−ペンチルホスフィン、
トリ−i−ブチルホスフィン、ジ−n−ブチルメチルホ
スフィン、トリシクロヘキシルホスフィン、1,2−ビス
(ジメチルホスフィノ)エタンなどの飽和脂肪族ホスフ
ィン類、トリアリルホスフィンなどの不飽和脂肪族ホス
フィン類、トリフェニルホスフィン、トリベンジルホス
フィン、ジ−i−プロピルフェニルホスフィン、ジビニ
ルフェニルホスフィン、n−ブチル−ジフェニルホスフ
ィンなどの芳香族ホスフィン類、1−エチルホスホラ
ン、1−フェニルホスホラン、1−フェニルホスファ
ン、1−フェニルホスフェパンなどの脂環式ホスフィン
類などを挙げることができる。
Examples of the phosphine as a raw material of the present invention include trimethylphosphine, diethylmethylphosphine, triethylphosphine, tri-n-propylphosphine, tri-n.
-Butylphosphine, tri-n-pentylphosphine,
Saturated aliphatic phosphines such as tri-i-butylphosphine, di-n-butylmethylphosphine, tricyclohexylphosphine, 1,2-bis (dimethylphosphino) ethane, unsaturated aliphatic phosphines such as triallylphosphine, Aromatic phosphines such as triphenylphosphine, tribenzylphosphine, di-i-propylphenylphosphine, divinylphenylphosphine, n-butyl-diphenylphosphine, 1-ethylphosphorane, 1-phenylphosphorane, 1-phenylphosphane And alicyclic phosphines such as 1-phenylphosphane and the like.

炭酸ジエステルとしては炭酸ジメチル、炭酸エチルメ
チル、炭酸ジエチル、炭酸ジプロピルなどを挙げること
ができるが、炭酸ジメチルなどのようにアルキル基の炭
素数が少ない方が四級化反応が速やかに進行し好まし
い。
Examples of the carbonic acid diester include dimethyl carbonate, ethylmethyl carbonate, diethyl carbonate, dipropyl carbonate, and the like, and the one having a smaller number of carbon atoms in the alkyl group such as dimethyl carbonate is preferable because the quaternization reaction proceeds rapidly.

無機酸としては、特に制約はないが、炭酸に比較し強
酸なものほど陰イオンへの交換は速く完結する。又、炭
酸に較べて弱い酸でも平衡を少しずつずらせながら行う
ことで時間をかければ陰イオン交換は達成される。これ
らの無機酸の具体的な例として、HF,HCl,HBr,HI,HNO3
H2SO4,H3PO4,H3BO3,HClO4,HBF4,HPF6,HSbF6,HAs
F6,HOSO2Cl,HOSO2F,H2CrO4,H2S2O6,HMnO4,HRe
O4,H2SeO4,HSCNなどを挙げることができる。
The inorganic acid is not particularly limited, but the stronger the acid is, the faster the exchange with anion is completed as compared with carbonic acid. In addition, even if the acid is weaker than carbonic acid, anion exchange can be achieved by shifting the equilibrium little by little and taking time. Specific examples of these inorganic acids include HF, HCl, HBr, HI, HNO 3 ,
H 2 SO 4 , H 3 PO 4 , H 3 BO 3 , HClO 4 , HBF 4 , HPF 6 , HSbF 6 , HAs
F 6 , HOSO 2 Cl, HOSO 2 F, H 2 CrO 4 , H 2 S 2 O 6 , HMnO 4 , HRe
O 4 , H 2 SeO 4 , HSCN and the like can be mentioned.

第1工程である四級化反応はホスフィン類と炭酸ジエ
ステルとのモル比で0.2〜5、より好ましくは0.3〜3と
し、溶媒の存在下又は非存在下、反応温度20〜200℃、
より好ましくは30〜160℃で実施される。通常ホスフィ
ン類が四級化物に充分転化したところで、未反応のホス
フィン類もしくは炭酸ジエステルを溶媒を用いた場合に
は溶媒とともに留去したのち、あるいは必要に応じて適
当な有機溶媒で再結晶して、第2工程に送られる。
The quaternization reaction which is the first step is carried out at a molar ratio of phosphines to carbonic acid diester of 0.2 to 5, more preferably 0.3 to 3, in the presence or absence of a solvent, a reaction temperature of 20 to 200 ° C.,
More preferably, it is carried out at 30 to 160 ° C. Usually, when the phosphine is sufficiently converted to a quaternary compound, the unreacted phosphine or the carbonic acid diester is distilled off together with the solvent when a solvent is used, or if necessary, recrystallized with a suitable organic solvent. , Sent to the second step.

第2工程では、四級ホスホニウム炭酸塩に通常量論値
に相当する無機酸を溶媒存在下又は非存在下に滴下し、
発生する炭酸ガスを減圧下又は不活性ガスを反応系に吹
き込むことで除去する。この際、起る反応は炭酸ジメチ
ルを原料とした場合、次式で表わされる。
In the second step, an inorganic acid corresponding to a normal stoichiometric value is added dropwise to the quaternary phosphonium carbonate in the presence or absence of a solvent,
The carbon dioxide gas generated is removed under reduced pressure or by blowing an inert gas into the reaction system. The reaction that occurs at this time is represented by the following equation when dimethyl carbonate is used as a raw material.

(式中、R1R2R3はホスフィンの炭化水素残基、Xは無機
酸の共役塩基を示す。) 反応後、副生アルコール及び溶媒を留去したのち得ら
れる固体が目的の四級ホスホニウム無機酸塩である。必
要に応じて適当な溶媒により再結晶などで高純度なもの
を得ることができる。
(In the formula, R 1 R 2 R 3 is a hydrocarbon residue of phosphine, and X is a conjugate base of an inorganic acid.) After the reaction, the by-produced alcohol and the solvent are distilled off, and the obtained solid is a quaternary compound. Phosphonium inorganic acid salt. If necessary, a highly pure product can be obtained by recrystallization or the like with an appropriate solvent.

又、炭酸イオンを完全に除くために量論値より少し過
剰な無機酸を使用した場合には、過剰の無機酸を再結晶
などの処理によって除くことができる。
Further, when an inorganic acid slightly in excess of the stoichiometric value is used to completely remove the carbonate ion, the excess inorganic acid can be removed by a treatment such as recrystallization.

〔発明の効果〕〔The invention's effect〕

本発明の方法によれば、効率的に各種の四級ホスホニ
ウム無機酸塩を製造することが可能であるが、同時に目
的とする塩を高純度で得ることができる点も本発明の大
きな特徴である。
According to the method of the present invention, it is possible to efficiently produce various quaternary phosphonium inorganic acid salts, but at the same time it is also a great feature of the present invention that the desired salt can be obtained in high purity. is there.

〔実施例〕〔Example〕

以下、実施例により本発明をさらに具体的に説明す
る。
Hereinafter, the present invention will be described in more detail with reference to Examples.

実施例−1 (第1工程) 攪拌式オートクレーブに炭酸ジメチル9.0g、トリ−n
−ブチルホスフィン18.5gを充てんし、反応温度115℃、
反応圧力5.0kg/cm2Gで15時間反応した。反応後オートク
レーブを冷却し、反応液を取り出してガスクロマトグラ
フで分析したところ、トリ−n−ブチルホスフィンの転
化率は72.8%であり、未反応物及び溶媒を留去したのち
の固体収量は17.5gであった(理論収率63.6%)。元素
分析並びに1H−NMRなどからこの固体はトリ−n−ブチ
ルメチルスホニウムテトラフルオロボレート10.1g(論
理収率92.4%、トリ−n−ブチルホスホニウム炭酸塩で
あることが確認された。
Example-1 (1st process) 9.0 g of dimethyl carbonates and tri-n were put into a stirring type autoclave.
-Filled with butylphosphine 18.5g, reaction temperature 115 ℃,
The reaction was carried out at a reaction pressure of 5.0 kg / cm 2 G for 15 hours. After the reaction, the autoclave was cooled, the reaction solution was taken out and analyzed by gas chromatography. The conversion rate of tri-n-butylphosphine was 72.8%, and the solid yield after distilling off unreacted materials and solvent was 17.5 g. Was (theoretical yield 63.6%). From the elemental analysis and 1 H-NMR, it was confirmed that this solid was 10.1 g of tri-n-butylmethylsulfonium tetrafluoroborate (theoretical yield: 92.4%, tri-n-butylphosphonium carbonate).

(第2工程) トリ−n−ブチルメチルホスホニウム炭酸塩10.0gを
水10.0gに溶解させ、42%HBF4水溶液7.9gを徐々に添
加、添加と同時に激しく炭酸ガスが発生した。より完全
に炭酸ガスを除去するために40℃/20mmHgで2時間脱
気、イオンクロマトグラフィーにより炭酸イオンが20pp
m以下であることを確認後、水を留去した。残渣を水−M
eOHの混合溶媒から再結晶するとトリ−n−ブチルメチ
ルホスホニウムテトラフルオロボレート10.1g(論理収
率92.4%、トリ−n−ブチルホスフィンに対し58.8%収
率)を得た。
(Second Step) 10.0 g of tri-n-butylmethylphosphonium carbonate was dissolved in 10.0 g of water, and 7.9 g of 42% HBF 4 aqueous solution was gradually added. At the same time, carbon dioxide gas was vigorously generated. Degassed at 40 ℃ / 20mmHg for 2 hours to completely remove carbon dioxide, and carbonate ion is 20pp by ion chromatography.
After confirming that it was not more than m, water was distilled off. The residue is water-M
Recrystallization from a mixed solvent of eOH gave 10.1 g of tri-n-butylmethylphosphonium tetrafluoroborate (theoretical yield 92.4%, 58.8% yield based on tri-n-butylphosphine).

実施例−2 (第1工程) 原料として炭酸ジメチル9.0g、トリエチルホスフィン
11.8g、メタノール10.0gを使用した以外は実施例−1第
1工程と同様の反応を行ったところ17.2gの固体を得た
(理論収率の78.9%)。元素分析、1H−NMRなどからこ
の固体はトリエチルメチルホスホニウム炭酸塩であるこ
とが確認された。
Example-2 (First step) 9.0 g of dimethyl carbonate and triethylphosphine as raw materials
When the same reaction as in Example 1 First Step was carried out except that 11.8 g and 10.0 g of methanol were used, 17.2 g of a solid was obtained (78.9% of theoretical yield). From elemental analysis, 1 H-NMR, etc., it was confirmed that this solid was triethylmethylphosphonium carbonate.

(第2工程) トリエチルメチルホスホニウム炭酸塩10.0g、42%HBF
4水溶液11.3g及び水10.0gを使用した以外は実施例−1
第2工程と同様の操作を行ったところトリエチルメチル
ホスホニウムテトラフルオロボレート10.8g(理論収率
の15.3%、トリエチルホスフィンに対し75.2%収率)を
得た。
(2nd step) Triethylmethylphosphonium carbonate 10.0g, 42% HBF
4 Example-1 except that 11.3 g of aqueous solution and 10.0 g of water were used
When the same operation as in the second step was carried out, 10.8 g of triethylmethylphosphonium tetrafluoroborate (15.3% of theoretical yield, 75.2% yield based on triethylphosphine) was obtained.

実施例−3 (第1工程) 原料として炭酸ジメチル9.0g、1−フェニルホスファ
ン17.8g、溶媒としてメタノール10.0gを使用した以外は
実施例−1第1工程と同様の反応を行ったところ、19.1
gの固体を得た(理論収率の71.3%)。元素分析、1H−N
MRなどからこの固体は1−メチルフェニルホスファニウ
ム炭酸塩であることが確認された。
Example-3 (First Step) A reaction similar to that of the first step of Example-1 was carried out except that 9.0 g of dimethyl carbonate, 17.8 g of 1-phenylphosphane were used as raw materials, and 10.0 g of methanol was used as a solvent. 19.1
g solid was obtained (71.3% of theoretical yield). Elemental analysis, 1 H-N
It was confirmed from MR and the like that this solid was 1-methylphenylphosphanium carbonate.

(第2工程) 1−メチルフェニルホスファニウム炭酸塩10.0gと60
%過塩素酸6.9g及び水10.0gを使用した以外は実施例−
1第2工程と同様の操作を行ったところ過塩素酸メチル
フェニルホスファニウム10.9g(理論収率の94.8%、1
−フェニルホスファンに対し67.6%収率)を得た。
(Second step) 1-methylphenylphosphanium carbonate 10.0 g and 60
% Except that 6.9 g of perchloric acid and 10.0 g of water were used.
When the same operation as in the 1st step 2 was performed, 10.9 g of methylphenylphosphanium perchlorate (94.8% of theoretical yield, 1
-67.6% yield based on phenylphosphane).

実施例−4 (第1工程) 原料として炭酸ジメチル9.0g、トリフェニルホスフィ
ン26.2g、溶媒とししてメタノール10.0gを使用した以外
は実施例−1第1工程と同様の反応を行ったところ21.3
gの固体を得た(理論収率60.5%)。元素分析、1H−NMR
などからこの固体はトリフェニルメチルホスホニウム炭
酸塩であることが確認された。
Example-4 (First Step) A reaction similar to that in the first step of Example-1 was carried out except that 9.0 g of dimethyl carbonate, 26.2 g of triphenylphosphine were used as raw materials, and 10.0 g of methanol was used as a solvent.
g of solid was obtained (theoretical yield 60.5%). Elemental analysis, 1 H-NMR
From the above, it was confirmed that this solid was triphenylmethylphosphonium carbonate.

(第2工程) トリフェニルメチルホスホニウム炭酸塩10.0gと60%
過塩素酸6.2g及びエタノール100gを使用した以外は実施
例−1第2工程と同様の操作を行ったところ過塩素酸ト
リフェニルメチルホスホニウム10.3g(論理収率の92.8
%、トリフェニルホスフィンに対し56.1%収率)を得
た。
(2nd step) Triphenylmethylphosphonium carbonate 10.0g and 60%
The same operation as in the second step of Example 1 was carried out except that 6.2 g of perchloric acid and 100 g of ethanol were used, and 10.3 g of triphenylmethylphosphonium perchlorate (the theoretical yield was 92.8 g).
%, 56.1% yield based on triphenylphosphine).

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】四級ホスホニウム無機酸塩を製造する方法
において、 (a)ホスフィン類を炭酸ジエステルと反応させ対応す
る四級ホスホニウム炭酸塩を製造する工程 (b)生成した四級ホスホニウム炭酸塩を無機酸と混合
して炭酸ガスを系外に除去せしめて対応する無機酸塩を
製造する工程 の2段階の工程を経ることを特徴とする四級ホスホニウ
ム無機酸塩の製造方法。
1. A method for producing a quaternary phosphonium inorganic acid salt, comprising the steps of: (a) reacting a phosphine with a carbonic acid diester to produce a corresponding quaternary phosphonium carbonate; (b) producing the quaternary phosphonium carbonate. A method for producing a quaternary phosphonium inorganic acid salt, which comprises performing a two-step process of producing a corresponding inorganic acid salt by removing carbon dioxide gas out of the system by mixing with an inorganic acid.
JP12542887A 1987-05-13 1987-05-22 Method for producing quaternary phosphonium inorganic acid salt Expired - Fee Related JPH0826053B2 (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP12542887A JPH0826053B2 (en) 1987-05-22 1987-05-22 Method for producing quaternary phosphonium inorganic acid salt
US07/192,524 US4892944A (en) 1987-05-13 1988-05-11 Process for producing quaternary salts
EP88107735A EP0291074B1 (en) 1987-05-13 1988-05-13 Process for producing quaternary salts
DE8888107735T DE3868138D1 (en) 1987-05-13 1988-05-13 METHOD FOR PRODUCING QUATERNAUS SALTS.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12542887A JPH0826053B2 (en) 1987-05-22 1987-05-22 Method for producing quaternary phosphonium inorganic acid salt

Publications (2)

Publication Number Publication Date
JPS63290890A JPS63290890A (en) 1988-11-28
JPH0826053B2 true JPH0826053B2 (en) 1996-03-13

Family

ID=14909855

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12542887A Expired - Fee Related JPH0826053B2 (en) 1987-05-13 1987-05-22 Method for producing quaternary phosphonium inorganic acid salt

Country Status (1)

Country Link
JP (1) JPH0826053B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE60320455T2 (en) * 2002-12-19 2009-06-18 Nippon Chemical Industrial Co., Ltd. ANTISTATIC FOR RESINS, ANTISTATIC RESIN COMPOSITIONS AND FORM BODY FROM ANTISTATIC RESINS
DE102004003958A1 (en) * 2004-01-26 2005-08-11 Basf Ag Production method for ionic liquids

Also Published As

Publication number Publication date
JPS63290890A (en) 1988-11-28

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