JPS6015610B2 - Process for producing acetic ester of unsaturated chlorine-containing alcohol - Google Patents

Process for producing acetic ester of unsaturated chlorine-containing alcohol

Info

Publication number
JPS6015610B2
JPS6015610B2 JP1122382A JP1122382A JPS6015610B2 JP S6015610 B2 JPS6015610 B2 JP S6015610B2 JP 1122382 A JP1122382 A JP 1122382A JP 1122382 A JP1122382 A JP 1122382A JP S6015610 B2 JPS6015610 B2 JP S6015610B2
Authority
JP
Japan
Prior art keywords
containing alcohol
chlorine
unsaturated
phosphoric acid
mol
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
Application number
JP1122382A
Other languages
Japanese (ja)
Other versions
JPS58128342A (en
Inventor
高在 湯本
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 JP1122382A priority Critical patent/JPS6015610B2/en
Publication of JPS58128342A publication Critical patent/JPS58128342A/en
Publication of JPS6015610B2 publication Critical patent/JPS6015610B2/en
Expired legal-status Critical Current

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  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

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酢酸ェステルの製法
で、その特徴とするところは一般式 (式中のR,およびR2は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酢酸
を80〜85%リン酸の存在で80〜95qoで反応せ
しめることによって、良収率で一般式 (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酢酸ェステルを製造
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 acetate ester of unsaturated chlorine-containing alcohol, and its characteristics are represented by the general formula (in the formula, R and R2 are hydrogen atoms or alkyl groups). By reacting unsaturated chlorine-containing alcohol and acetic anhydride at 80 to 95 qo in the presence of 80 to 85% phosphoric acid, the general formula (R and R2 in the formula have the same meanings as above) can be obtained in good yield. The present invention relates to a method for producing an acetate ester of an unsaturated chlorine-containing alcohol.

本発明者は不飽和舎塩素アルコールのアセチル化につい
て研究し、原料の不飽和含塩素アルコールのアセチル化
の際に添加する助剤による脱水あるいは樹脂化反応を防
止して、良好な収率で不飽和含塩素アルコールの酢酸ェ
ステルの合成法について鋭意検討した結果、不飽和含塩
素アルコールと無水酢酸の混合物にリン酸を低温で添加
した後加熱反応せしめて、脱水によるジェン化合物を生
成することなく目的のアセチル化物を純度よく良収率で
製造する方法を見出した。
The present inventor has researched the acetylation of unsaturated chlorine-containing alcohol, and has prevented the dehydration or resinization reaction by using an auxiliary agent added during acetylation of unsaturated chlorine-containing alcohol as a raw material. As a result of intensive research on a method for synthesizing acetate ester of saturated chlorinated alcohol, we found that phosphoric acid was added to a mixture of unsaturated chlorinated alcohol and acetic anhydride at low temperature, and then the reaction was carried out by heating. We have discovered a method for producing an acetylated product with high purity and good yield.

アルコール類のヒドロキシル基をアセチル化する場合、
アセチル化試剤として、酢酸、無水酢酸塩化アセチルな
どを種々の助剤ととも‘こ用いる方法がとられている。
When acetylating the hydroxyl group of alcohols,
As the acetylation reagent, acetic acid, acetyl anhydride, acetyl chloride, and the like are used together with various auxiliaries.

不飽和含塩素アルコールをアセチル化する場合、いよい
よ原料の脱水によるジェン化合物の生成をともない、目
的のアセチル化物を純度よく良収率で得ることが驚かし
い。本発明者の方法によるアセチル化方法は、源料の不
飽和舎塩素アルコールの脱水によるジェン化合物の生成
および樹脂化を防止するため、アセチル化謎剤として無
水酢酸を助剤として80〜85%リン酸を使用すること
によって、これらの欠点を改良した方法である。不館和
含塩素アルコールに対するアセチル化謎剤の無水酢酸の
割合は1モル当り10モルまでである。
When unsaturated chlorine-containing alcohol is acetylated, it is surprising that the desired acetylated product can be obtained in high purity and in good yield, with the production of a diene compound by dehydration of the raw material. The acetylation method according to the present inventor's method uses acetic anhydride as an acetylation mystery agent as an auxiliary agent in order to prevent the formation of a compound and resin formation due to dehydration of the unsaturated chlorine alcohol as a raw material. This method improves these drawbacks by using an acid. The ratio of acetic anhydride as the acetylated mystery agent to the chlorine-containing alcohol is up to 10 moles per mole.

しかし無水酢酸の使用量としては5〜6モルが適当であ
る。添加する助剤のリン酸は、リン、メタリン酸、ポリ
リン酸などを単独または併して用いることができる。脱
水され易い構造をする化合物については純度の高いリン
酸は不可、一般に80〜85%までのリン酸が適当であ
る。ェステル化の触媒としてリン酸を用いる場合に注、
しなければならないのは、原料アルコールの脱によるジ
ヱン化合物の生成である。また生成しこジェン化合物は
ェステルと分離が困難であるた、純度の高いェステスを
得る条件が求められる。この目的には温和なリン酸が適
しているが亀陰性度の強い塩素原子を有するため、適当
な渡のリン酸と反応温度が用いられる。リン酸濃度低い
場合及び反応温度の低い場合原料が未反応}残り好まし
くない。別表に含塩素アルコール0.1モルに無水酢酸
0.6ルを添加し、85%リン酸0.046モルを0〜
5℃い添加した後濠裕上で異なる温度で加熱反応せした
結果及び他の触媒を用いた場合の収率を比較したが、リ
ン酸濃度80〜85%、反応温度80〜95℃yま良収
率で純度の高いェステルが得られた。別 表リン酸の添
加量は不飽和含塩素アルコールに対して1〜100重量
%である。
However, the appropriate amount of acetic anhydride to be used is 5 to 6 moles. As the auxiliary phosphoric acid to be added, phosphorus, metaphosphoric acid, polyphosphoric acid, etc. can be used alone or in combination. For compounds that have a structure that is easily dehydrated, highly pure phosphoric acid is not possible, and 80-85% phosphoric acid is generally suitable. Note when using phosphoric acid as a catalyst for esterification,
What must be done is to generate a diene compound by eliminating the raw material alcohol. Furthermore, since it is difficult to separate the produced thiogen compound from the ester, conditions for obtaining a highly pure ester are required. Although mild phosphoric acid is suitable for this purpose, since it has a chlorine atom with strong heminegative properties, an appropriate range of phosphoric acid and reaction temperature is used. If the phosphoric acid concentration is low or the reaction temperature is low, raw materials may remain unreacted, which is not preferable. In the attached table, add 0.6 liters of acetic anhydride to 0.1 mol of chlorinated alcohol, and add 0.046 mols of 85% phosphoric acid to 0.1 mols of chlorinated alcohol.
We compared the results of heating reactions at different temperatures on a moat after addition at 5°C and the yields when using other catalysts. A high purity ester was obtained in good yield. The amount of phosphoric acid added is 1 to 100% by weight based on the unsaturated chlorine-containing alcohol.

リン酸の添加量の多い場合はジヱン化合物が生成するた
め、条件によって極力低くおさえる。またリン酸は低温
0〜1000以内で添加すべきで、1ぴ0以上の条件で
はジヱン化合物の生成および樹脂化の原因となる。助剤
添加後の加熱時間は1〜1Q時間で充分で、通常3時間
以内で反応は完了する。加熱時間が長びけば、ジェン化
合物などの生成の原因となる。
If the amount of phosphoric acid added is large, a diene compound will be produced, so it should be kept as low as possible depending on the conditions. Further, phosphoric acid should be added at a low temperature of 0 to 1,000 ℃, and if the temperature is 1 to 0 or higher, it will cause the formation of diene compounds and resin formation. A heating time of 1 to 1Q hours after addition of the auxiliary agent is sufficient, and the reaction is usually completed within 3 hours. If the heating time is prolonged, it may cause generation of gen compounds and the like.

本発明のェステルは、有機合成中間体、農薬、食誘引剤
および雛燃処理剤などの原料として有用である。
The ester of the present invention is useful as a raw material for organic synthesis intermediates, agricultural chemicals, food attractants, chick burning 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 1 CC12=CCIC比OH16.17夕(0.10モル
)と無水酢酸61.25夕(0.60モル)の混合物を
0〜5℃に冷却しておき、これに85%リン酸4.5夕
(0.039モル)を30分で滴下する。
Example 1 CC12=CCIC ratio A mixture of OH16.17 (0.10 mol) and acetic anhydride 61.25 (0.60 mol) was cooled to 0-5°C, and 85% phosphoric acid 4 0.5 mol (0.039 mol) was added dropwise over 30 minutes.

その間反応温度は正しく5℃以下に保つ。滴下後傷裕上
(約90〜95oo)で3時間加熱反応させる。反応混
合物を氷水中に投入分解し、四塩化炭素で数回抽出する
。四塩化炭素溶液を酸性水素ナトリウム溶液および食塩
の飽和水溶液で洗った後塩化カルシウムで乾燥する。四
塩化炭素を回収し、槌油19.87夕を得た。粗油を分
留しbp74.5〜76.0oo/8肋Hg(d葦ol
.4130、n勢1.4873塩素含有率52.25%
)の不飽和ヱステルCH3C0・OCH2CCI=CC
12を15.97夕(78.4%)を得た。実施例 2 17.54夕(0.10モル)と 無水酢酸61.25夕(0.06モル)の混合液を0〜
5℃に冷却しておき、この混合液に85%リン酸4.5
夕(0.039モル)を30分間で滴下する。
During this time, the reaction temperature is kept properly below 5°C. After dropping, the mixture is heated and reacted for 3 hours at a temperature of about 90 to 95 oo. The reaction mixture was decomposed in ice water and extracted several times with carbon tetrachloride. The carbon tetrachloride solution is washed with an acidic sodium hydrogen solution and a saturated aqueous solution of common salt, and then dried over calcium chloride. Carbon tetrachloride was recovered to obtain 19.87 ml of hammer oil. The crude oil was fractionated to bp74.5-76.0oo/8 Hg (d reed ol
.. 4130, n force 1.4873 chlorine content 52.25%
) unsaturated ester CH3C0・OCH2CCI=CC
12 was obtained in 15.97 days (78.4%). Example 2 A mixed solution of 17.54 mmol (0.10 mol) and acetic anhydride 61.25 mmol (0.06 mol) was
Cool to 5°C and add 4.5% 85% phosphoric acid to this mixture.
(0.039 mol) was added dropwise over 30 minutes.

滴下後さらに湯浴上で3時間加熱反応させる。反応後混
合物を氷水中に投入分解し、四塩化炭素で抽出する。抽
出液を酸性水素ナトリウムおよび食塩の飽和溶液で洗っ
たのち乾燥する。溶媒を蟹去して残油20.39夕を得
た。この油分を分留してbp71.0〜72.0oo/
8側Hg(d葦ol.3斑7、nきol.4784、塩
素含有率48.73%)の不飽和ェステル18.47夕
(収率縄.9 %)を得た。
After the dropwise addition, the mixture was further heated and reacted on a hot water bath for 3 hours. After the reaction, the mixture was decomposed in ice water and extracted with carbon tetrachloride. The extract is washed with a saturated solution of sodium hydrogen acid and common salt and then dried. The solvent was removed to obtain a residual oil of 20.39 g. This oil is fractionated and has a bp of 71.0 to 72.0oo/
18.47 unsaturated esters (yield: .9%) of 8-side Hg (reed ol. 3 spots 7, nickel ol. 4784, chlorine content 48.73%) were obtained.

実施例 3 18.94夕(0.10モル) と無水酢酸61.25夕(0.60モル)の混合液を0
〜5℃に冷却しておき、この混合液に85%リン酸4.
5夕(0.039モル)を30分で滴下する。
Example 3 A mixed solution of 18.94 mmol (0.10 mol) and acetic anhydride 61.25 mmol (0.60 mol) was
Cool to ~5°C and add 4.85% phosphoric acid to this mixture.
5 (0.039 mol) was added dropwise over 30 minutes.

滴下後さらに湯浴上で3時間加熱反応させる。反応後実
施例1と同様に処理して四塩化炭素抽出液を得る。四塩
化炭素を回収して残油20.56夕を得た。これを分留
してbp79.0〜83.000/8側Hg(d葦ol
.295ふ n色ol.478う塩素含有率45.87
%)の不飽和ェステル18.57夕 (収率75.6%)を得た。
After the dropwise addition, the mixture was further heated and reacted on a hot water bath for 3 hours. After the reaction, the same treatment as in Example 1 is carried out to obtain a carbon tetrachloride extract. Carbon tetrachloride was recovered to obtain 20.56 ml of residual oil. This was fractionated and bp79.0~83.000/8 side Hg (d reed ol
.. 295fu n color ol. 478 Chlorine content rate 45.87
%) of unsaturated ester (yield 75.6%) was obtained.

実施例 4 6.07夕(0.03モ ル)と無水酢酸30.62夕(0.30モル)の混合液
を0〜5℃に冷却しておき、この混合液に85%リン酸
2.22(0.019モル)を3び分で滴下する。
Example 4 A mixture of 6.07 mm (0.03 mol) and acetic anhydride (0.30 mol) was cooled to 0 to 5°C, and 2.0 mm of 85% phosphoric acid was added to this mixture. 22 (0.019 mol) was added dropwise in 3 portions.

滴下後さらに湯浴上で3時間加熱反応させる。反応後実
施例1と同様に処理して四塩化炭素抽出液を得る。四塩
化炭素を蟹去した後残油7.52夕を得た。残油を分留
してbp88.0〜89.0℃/8脚Hg(d葦。1.
250い n色ol.476ふ塩素含有率43.13%
)の留分6.71夕(収率91.6%)を得た。
After the dropwise addition, the mixture was further heated and reacted on a hot water bath for 3 hours. After the reaction, the same treatment as in Example 1 is carried out to obtain a carbon tetrachloride extract. After removing the carbon tetrachloride, 7.52 g of residual oil was obtained. The residual oil was fractionated and bp88.0-89.0℃/8 legs Hg (d reed.1.
250 n color ol. 476F chlorine content 43.13%
6.71 fractions (yield 91.6%) of ) were obtained.

Claims (1)

【特許請求の範囲】 1 一般式 ▲数式、化学式、表等があります▼ (式中のR_1およびR_2は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
酢酸を80〜85%リン酸の存在で80〜95℃で反応
せしめることを特徴とする 一般式 ▲数式、化学式、表等があります▼ (式中のR_1およびR_2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酢酸エステルの
製法。
[Claims] 1. Unsaturated chlorine-containing alcohol and acetic anhydride represented by the general formula ▲ Numerical formulas, chemical formulas, tables, etc. ▼ (R_1 and R_2 in the formula are hydrogen atoms or alkyl groups) General formula▲There are mathematical formulas, chemical formulas, tables, etc.▼ (R_1 and R_2 in the formula have the same meanings as above)
A method for producing acetic ester of unsaturated chlorine-containing alcohol represented by
JP1122382A 1982-01-27 1982-01-27 Process for producing acetic ester of unsaturated chlorine-containing alcohol Expired JPS6015610B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1122382A JPS6015610B2 (en) 1982-01-27 1982-01-27 Process for producing acetic ester of unsaturated chlorine-containing alcohol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1122382A JPS6015610B2 (en) 1982-01-27 1982-01-27 Process for producing acetic ester of unsaturated chlorine-containing alcohol

Publications (2)

Publication Number Publication Date
JPS58128342A JPS58128342A (en) 1983-07-30
JPS6015610B2 true JPS6015610B2 (en) 1985-04-20

Family

ID=11771957

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1122382A Expired JPS6015610B2 (en) 1982-01-27 1982-01-27 Process for producing acetic ester of unsaturated chlorine-containing alcohol

Country Status (1)

Country Link
JP (1) JPS6015610B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH022612U (en) * 1988-06-17 1990-01-09

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH022612U (en) * 1988-06-17 1990-01-09

Also Published As

Publication number Publication date
JPS58128342A (en) 1983-07-30

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