JPS58128341A - Preparation of propionic ester from unsaturated alcohol containing chlorine - Google Patents

Preparation of propionic ester from unsaturated alcohol containing chlorine

Info

Publication number
JPS58128341A
JPS58128341A JP57011224A JP1122482A JPS58128341A JP S58128341 A JPS58128341 A JP S58128341A JP 57011224 A JP57011224 A JP 57011224A JP 1122482 A JP1122482 A JP 1122482A JP S58128341 A JPS58128341 A JP S58128341A
Authority
JP
Japan
Prior art keywords
phosphoric acid
acid
unsaturated alcohol
unsaturated
containing chlorine
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
JP57011224A
Other languages
Japanese (ja)
Other versions
JPS6014011B2 (en
Inventor
Takaari Yumoto
湯本 高在
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP57011224A priority Critical patent/JPS6014011B2/en
Publication of JPS58128341A publication Critical patent/JPS58128341A/en
Publication of JPS6014011B2 publication Critical patent/JPS6014011B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To obtain the titled substance useful as a raw material for organic synthetic intermediates, agricultural chemicals, food-type attractants and flame retardants, etc. in high purity and yield, by reacting an unsaturated alcohol containing chorine with propionic acid anhydride in the presence of phosphoric acid. CONSTITUTION:Phosphoric acid as an assistant is added to a mixture of an unsaturated alcohol, containing chlorine, and expressed by formulaI(R1 and R2 are H or alkyl) is reacted with propionic acid anhydride (an esterification reagent) at a low temperature (0-10 deg.C), and the reaction is carried out under heating to suppress the formation of diene compounds and resinification by side reactions and obtain advantageously the compound of formula II. Phosphoric acid, metaphosphoric acid and polyphosphoric acid can be used alone or together, and phosphoric acid of high purity is unsuitable for an easily dehydrated compound. Generally, phosphoric acid of up to 85% purity is suitable.

Description

【発明の詳細な説明】 本発明は不飽和含塩素アルコールのプロピオン酸エステ
ルの製法で、その特徴とするところは一般式 C]−R2水素原子またはアルキ ル基である) で表わされる不飽和含塩素アルコールと無水プロピオン
酸をリン酸の存在で反応せしめることによって 一般式 %式% (式中のE、およびR2は前記と同じ意味を持つ)で表
わされる不飽和含塩素アルコールのプロピオン酸エステ
ルを製造する方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention is a method for producing a propionate ester of an unsaturated chlorine-containing alcohol, which is characterized by an unsaturated chlorine-containing ester represented by the general formula C]-R2 (hydrogen atom or alkyl group). Producing propionic acid ester of unsaturated chlorine-containing alcohol represented by the general formula % (in which E and R2 have the same meanings as above) by reacting alcohol and propionic anhydride in the presence of phosphoric acid. It's about how to do it.

本発明者は不飽和含塩素アルコールのエステル化試剤お
よび助剤について研究し、原料の不飽和含塩素アルコー
ルが添加した助剤によって、脱水あるいは樹脂化するた
め、これらの反応を防いで良収率で不飽和含塩素アルコ
ールのプロピオン酸エステルを得今方法について種4検
的した結果、不飽和含塩素アルコールと無水プロピオン
酸の混合液にリン酸を低温で添加した後、さらに加熱反
応させることによって、副生するジエン化合物の生成を
防ぎ目的のエステルを純度よく高収率で製造する方法を
見出した。
The present inventor has researched esterification reagents and auxiliary agents for unsaturated chlorinated alcohol, and found that since the raw material unsaturated chlorinated alcohol is dehydrated or turned into a resin by the added auxiliary agent, these reactions can be prevented and high yields achieved. The propionic acid ester of an unsaturated chlorine-containing alcohol was obtained using the following method.As a result of the present method, it was found that by adding phosphoric acid to a mixture of an unsaturated chlorine-containing alcohol and propionic anhydride at a low temperature, and then further heating the reaction. discovered a method for producing the desired ester with high purity and high yield by preventing the formation of by-product diene compounds.

アルコール類のヒドロキシル基を10ピオニル化してプ
ロピオン酸エステルを製造する場合、エステル化試剤と
して、プロピオン酸、無水プロピオン酸および塩化プロ
ピオニルなどとともに種々の助剤が用いられる。プロピ
オニlし化する物質によっては試剤と助剤の組合せを選
択する必要がある。不飽和含塩素アルコールのプロピオ
ニル化に際して脱水、樹脂化などの副反応を起し易く、
ジエン化合物などの副生物を生成することなく純度よく
高収率で目的のエステルを得ることが難かしい。
When a propionic acid ester is produced by depyonylating a hydroxyl group of an alcohol, various auxiliary agents are used as an esterification agent together with propionic acid, propionic anhydride, propionyl chloride, and the like. Depending on the substance to be propionized, it is necessary to select a combination of reagents and auxiliary agents. When propionylating unsaturated chlorine-containing alcohols, side reactions such as dehydration and resin formation are likely to occur.
It is difficult to obtain the desired ester with good purity and high yield without producing by-products such as diene compounds.

本発明者の方法によるエステル化試剤(無水)”ロビオ
ン酸)と助剤(リン酸)の組合せは、副生ずるジエン化
合物の4ト成および樹脂化を充分に防1にでき、他の試
剤と助剤を用いる方法の欠点を改めたものである。
The combination of the esterification reagent (anhydride) ``robionic acid'' and the auxiliary agent (phosphoric acid) according to the method of the present inventor can sufficiently prevent the four-tone formation and resin formation of the diene compound produced as a by-product, and can be used in combination with other reagents. This method corrects the drawbacks of the method using auxiliary agents.

本発明方法によれば、原料の不飽和含塩素アルコールに
対するエステル化試剤の無水プロピオン酸の割合は/七
ル当り10モ)vまでである。しかし無水プロピオン酸
の使用量は通常S〜乙モル当量が適当である。
According to the method of the invention, the ratio of propionic anhydride as an esterifying agent to unsaturated chlorine-containing alcohol as a raw material is up to 10 mo)/7 liters. However, the appropriate amount of propionic anhydride to be used is usually an S to O molar equivalent.

また添加する助剤のリン酸は、リン酸、メタリン酸およ
びポリリン酸を単独または併用して用いることができる
。特に脱水され易い構造を有する化合物については純度
の高いリン酸は不適当で、一般にg5%までのリン酸が
適当である。
Further, as the auxiliary phosphoric acid to be added, phosphoric acid, metaphosphoric acid, and polyphosphoric acid can be used alone or in combination. For compounds having structures that are particularly susceptible to dehydration, highly pure phosphoric acid is inappropriate, and phosphoric acid of up to 5% g is generally suitable.

リン酸の添加量は、不飽和含塩素アルコールに苅して/
〜700重量%程度で充分で、リン酸の添加量の多い場
合にはジエン化合物が副生ずるだめ、極力低くおさえる
事が必要である。捷たリン酸添加時の温度は0〜10°
C以内が適当で70°C以−にでは同様にジエン化合物
の生成および樹脂化が促進される。
The amount of phosphoric acid added is determined by adding it to unsaturated chlorine-containing alcohol.
About 700% by weight is sufficient, and if the amount of phosphoric acid added is large, diene compounds will be produced as by-products, so it is necessary to keep it as low as possible. The temperature when adding crushed phosphoric acid is 0 to 10°
A temperature of less than 70°C is suitable, and a temperature of 70°C or higher similarly promotes the formation of diene compounds and resin formation.

エステル化試剤に助剤を加え終った後の加熱時間は7〜
70時間が適当で、通常3時間以内で反応が完了する。
The heating time after adding the auxiliary agent to the esterification reagent is 7~
A suitable time is 70 hours, and the reaction is usually completed within 3 hours.

反応時間は短いほど良好で、長ければジエン化合物など
の生成の原因となる。
The shorter the reaction time, the better; if the reaction time is longer, diene compounds and the like may be generated.

本発明方法により得られるエステルは、有機合成中間体
、農薬、全誘引剤および難燃処理剤などの原料として有
用である。
The ester obtained by the method of the present invention is useful as a raw material for organic synthesis intermediates, agricultural chemicals, total attractants, flame retardant treatment agents, and the like.

以下の実施例によって本発明を具体的に説明する。The present invention will be specifically explained by the following examples.

実施例/ CCI□=CClCH20Hg、 079 (00,!
;−r= w )と無水プロピオン酸39.0!;yC
030モル)の混合液を0−5 ’Cに冷却したのちg
s%リン酸2.2乙fZ<、00/タモル)を30分間
で滴−卜する。
Example/CCI□=CClCH20Hg, 079 (00,!
;-r=w ) and propionic anhydride 39.0! ;yC
After cooling a mixture of 030 mol) to 0-5'C, g
s% phosphoric acid (2.2% fZ<,00/tamol) was added dropwise over 30 minutes.

滴下後さらに湯浴1 (70〜95”C)で3時間加熱
反応させる。反応混合液を氷水中に投入分解したのち、
四塩化炭素で抽出する。抽出液は酸性水素ナトリウム水
溶液および塩化ナトリウムの飽和水溶液で洗ったのち乾
燥する。抽出液より四塩化炭素を回収し、粗油/41.
0/9を得た。粗油を分留L bp 乙3.0〜A l
、、 0°C/3mmHg、 (d、”73グ、!0、
)?:/グg/2、塩素含有率41g乙j%)のエステ
ル C■]3CH2CO・0CH2CC工二CCl2留分3
309(収率乙90%)を得た。
After the dropwise addition, the mixture was further heated and reacted in hot water bath 1 (70 to 95"C) for 3 hours. The reaction mixture was placed in ice water and decomposed, and then
Extract with carbon tetrachloride. The extract is washed with an acidic sodium hydrogen aqueous solution and a saturated sodium chloride aqueous solution and then dried. Carbon tetrachloride is recovered from the extract and crude oil/41.
Got 0/9. Fractional distillation of crude oil L bp Otsu 3.0 ~ A l
,, 0°C/3mmHg, (d,”73g,!0,
)? :/g/2, chlorine content 41g%) ester C]3CH2CO・0CH2CCCCl2 fraction 3
309 (yield Otsu 90%) was obtained.

実施例2 13 CCI2 =CC1−CHOHI7.!;’19  (
010モ ル )と無水プロピオン酸71!i>0り9
CO乙0モル)の混合液をo = s ’cに冷却した
のち、gs%リン酸41.3−I9(0039モル)を
30分間で滴下する。
Example 2 13 CCI2 =CC1-CHOHI7. ! ;'19 (
010 mol) and propionic anhydride 71! i>0ri9
After cooling the mixed solution of CO (0 mol) to o = s'c, gs% phosphoric acid 41.3-I9 (0039 mol) was added dropwise over 30 minutes.

滴下後、さらに湯浴」二で3時間反応させる。反応後、
反応混合液を氷水中に投入分解したのち四塩化炭素で抽
出する。抽出液は実施例/に示すように洗浄、乾燥後、
四塩化炭素を回収し、粗油3グ’729を得た。粗油を
分留してbp3/、0〜S20°C/、2W肩Hg <
 4”  y、 、2y 乙3、h:/グア乙01塩素
含有率4t!;、941%)の不飽和工01(3 1 ステルC1(3CH2Co−0−ell(−CC工=C
C上z/3332(収率707%)を得た。
After dropping, the mixture was further reacted in a hot water bath for 3 hours. After the reaction,
The reaction mixture was decomposed in ice water and then extracted with carbon tetrachloride. After washing and drying the extract as shown in Example/
Carbon tetrachloride was recovered and crude oil 3g'729 was obtained. Crude oil is fractionated to bp3/, 0~S20°C/, 2W shoulder Hg <
4"y, ,2y Otsu3, h:/Gua Otsu01 chlorine content 4t!;,941%) unsaturated 01(3 1 Stell C1(3CH2Co-0-ell(-CC=C
C z/3332 (yield 707%) was obtained.

実施例3 crt□CI:’f3 CCl2 =CC1−CI”JOl−11g、9 3 
 y−(0/  0  モ ル )ト無水プロピオン酸
7g09y(060モル)の混合液をθ〜3 ’Cに冷
却したのちg5%リン酸グS/り(0039モル)を3
0分間で滴下する。
Example 3 crt□CI:'f3 CCl2 =CC1-CI"JOl-11g, 9 3
After cooling a mixture of 7 g09y (060 mol) of y-(0/0 mol) propionic anhydride to θ~3'C, 3 g5% phosphoric acid S/ri (0039 mol) was added.
Drop in 0 minutes.

滴下後さらに温浴上で3時間反応させる。反応混合液を
氷水中に投入分解し、四塩化炭素で抽出する。抽出液は
実施例/に示すように洗汀1、乾燥後四塩化炭素を回収
し粗油3g2θyを得た。粗油を分留しbp乙go−乙
g3°C/3關IQ; (d、”/2乙09、)17/
グアS乙、塩素含有率グ327%)の不飽和エステル CH2CH3 CH3CH2C0・OCH−CC,にCC上2  i3
乙5F(収率乙9S%)を得た。
After the dropwise addition, the reaction was continued for 3 hours on a hot bath. The reaction mixture was decomposed in ice water and extracted with carbon tetrachloride. The extract was washed 1 and dried as shown in Example 1, and then carbon tetrachloride was recovered to obtain 3g2θy of crude oil. Fractionally distill the crude oil and bp Otsugo-Otsug3°C/3關IQ; (d,”/2Otsu09,)17/
Gua S, chlorine content 327%) unsaturated ester CH2CH3 CH3CH2C0・OCH-CC, CC on 2 i3
Otsu 5F (yield Otsu 9S%) was obtained.

実施例り CH2CH2CH3 CC1,、=  CC]−−CIiO)I  2033
 9  (0/  0 モ tv)と無水プロピオン酸
7gO?ICO乙Oモ/I/)の混合液を0〜3°Cに
冷却したのちg5%リン酸クグり!(003タモル)を
30分間で滴下する。
Example CH2CH2CH3 CC1,, = CC]--CIiO)I 2033
9 (0/0 mo tv) and propionic anhydride 7gO? After cooling the mixture of ICO Otsu Omo/I/) to 0-3°C, add g5% phosphoric acid! (003 tamole) was added dropwise over 30 minutes.

滴下後賜浴」−で3時間加熱反応させる。反応混合液を
氷水中に投入分解したのち、四塩化炭素で抽出する。抽
出液は実施例/に示すように洗浄、乾燥後四塩化炭素を
回収する。粗油22329を得た。粗油を分留しbpg
7o〜KgK”C/3朋Hg(da’  123 乙A
、)t:  /、11739)塩素含有率りog41%
)の不飽和エステル CH2CH2C■(3 唱 CF2Cl(□CO,OCR−CC]−二CC]−2/
左3に2(収率Sゾ2%)を得た。
After the dropwise addition, the mixture was heated and reacted in a bath for 3 hours. The reaction mixture was decomposed in ice water, and then extracted with carbon tetrachloride. The extract is washed and dried as shown in Example 1, and then carbon tetrachloride is recovered. Crude oil 22329 was obtained. Fractional distillation of crude oil to bpg
7o~KgK"C/3hoHg(da' 123 Otsu A
,) t: /, 11739) Chlorine content rate og41%
) unsaturated ester CH2CH2C■(3 CF2Cl(□CO,OCR-CC]-2CC]-2/
2 (yield S zo 2%) was obtained on the left.

Claims (1)

【特許請求の範囲】 一般式 %式% ) で表わされる不飽和含塩素アルコールと無水プロピオン
酸をリン酸の存在で反応せしめることを特徴とする 一般式 (式中のR]およびR2は前記と同じ意味を持つ)で表
わされる不飽和含塩素アルコールのプロピオン酸エステ
ルの製法。
[Scope of Claims] A general formula characterized in that an unsaturated chlorine-containing alcohol represented by the general formula % and propionic anhydride are reacted in the presence of phosphoric acid (R in the formula and R2 are as above) A process for producing propionate esters of unsaturated chlorine-containing alcohols, which have the same meaning.
JP57011224A 1982-01-27 1982-01-27 Process for producing propionic acid ester of unsaturated chlorine-containing alcohol Expired JPS6014011B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57011224A JPS6014011B2 (en) 1982-01-27 1982-01-27 Process for producing propionic acid ester of unsaturated chlorine-containing alcohol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57011224A JPS6014011B2 (en) 1982-01-27 1982-01-27 Process for producing propionic acid ester of unsaturated chlorine-containing alcohol

Publications (2)

Publication Number Publication Date
JPS58128341A true JPS58128341A (en) 1983-07-30
JPS6014011B2 JPS6014011B2 (en) 1985-04-11

Family

ID=11771983

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57011224A Expired JPS6014011B2 (en) 1982-01-27 1982-01-27 Process for producing propionic acid ester of unsaturated chlorine-containing alcohol

Country Status (1)

Country Link
JP (1) JPS6014011B2 (en)

Also Published As

Publication number Publication date
JPS6014011B2 (en) 1985-04-11

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