JPH1045710A - Production of 3-chloro-1-thiocyanate-2-propene - Google Patents

Production of 3-chloro-1-thiocyanate-2-propene

Info

Publication number
JPH1045710A
JPH1045710A JP8207046A JP20704696A JPH1045710A JP H1045710 A JPH1045710 A JP H1045710A JP 8207046 A JP8207046 A JP 8207046A JP 20704696 A JP20704696 A JP 20704696A JP H1045710 A JPH1045710 A JP H1045710A
Authority
JP
Japan
Prior art keywords
chloro
dichloropropene
propene
phase transfer
transfer catalyst
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.)
Pending
Application number
JP8207046A
Other languages
Japanese (ja)
Inventor
Hideki Matsuda
英樹 松田
Goro Asanuma
五朗 浅沼
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.)
Kuraray Co Ltd
Original Assignee
Kuraray 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 Kuraray Co Ltd filed Critical Kuraray Co Ltd
Priority to JP8207046A priority Critical patent/JPH1045710A/en
Priority to IN276CA1997 priority patent/IN182219B/en
Priority to AU14819/97A priority patent/AU690866B2/en
Priority to AT97102811T priority patent/ATE228509T1/en
Priority to DE69717330T priority patent/DE69717330T2/en
Priority to EP97102811A priority patent/EP0794180B1/en
Priority to CN97109983A priority patent/CN1073096C/en
Priority to US08/804,401 priority patent/US5894073A/en
Publication of JPH1045710A publication Critical patent/JPH1045710A/en
Priority to US09/225,292 priority patent/US6103921A/en
Priority to US09/545,349 priority patent/US6222057B1/en
Priority to US09/547,221 priority patent/US6245927B1/en
Pending 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

PROBLEM TO BE SOLVED: To industrially and readily obtain the subject compound useful as a synthetic intermediate for agrochemicals in a high yield by using a specific catalyst when 1,3-dichloropropene is reacted with a thiocyanic aid salt in an organic solvent. SOLUTION: 1,3-Dichloropropene is reacted with a thiocyanic acid salt in an organic solvent in the presence of a phase transfer catalyst. A quaternary ammonium salt, a quaternary phosphonium salt, especially tetramethyl ammonium chloride, tetraethyl ammonium chloride, tetrabutyl ammonium chloride, etc., is preferable as the phase transfer catalyst. The phase transfer catalyst is preferably used in an amount of 0.001-0.01mol based on 1mol 1,3- dichloropropene. The organic solvent includes e.g. diisopropyl ether or toluene. 3-Chloro-1-thiocynate-2-propene is useful as a synthetic intermediate for hexahydrotriazine compound useful as an insecticide.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、3−クロロ−1−
チオシアナト−2−プロペンの製造法に関する。本発明
により製造される3−クロロ−1−チオシアナト−2−
プロペンは、農薬等の合成中間体として有用である。
[0001] The present invention relates to 3-chloro-1-
The present invention relates to a method for producing thiocyanato-2-propene. 3-Chloro-1-thiocyanato-2- produced according to the present invention
Propene is useful as a synthetic intermediate for agricultural chemicals and the like.

【0002】[0002]

【従来の技術】3−クロロ−1−チオシアナト−2−プ
ロペンの製造法としては、1,3−ジクロロプロペンと
チオシアン酸カリウムをジメチルスルホキシド中で反応
させる方法(Journal f. prakt. Chemie. Band 322, He
ft 4, 1980, S, 629参照)が知られている。
2. Description of the Related Art As a method for producing 3-chloro-1-thiocyanato-2-propene, 1,3-dichloropropene is reacted with potassium thiocyanate in dimethyl sulfoxide (Journal f. Prakt. Chemie. Band 322). , He
ft 4, 1980, S, 629).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
方法における3−クロロ−1−チオシアナト−2−プロ
ペンの収率は47%と低く、かかる方法は工業的に有利
な製造方法とはいい難い。しかして、本発明の目的は、
工業的に容易に、かつ高収率で3−クロロ−1−チオシ
アナト−2−プロペンを製造する方法を提供することに
ある。
However, the yield of 3-chloro-1-thiocyanato-2-propene in the above method is as low as 47%, and such a method is not an industrially advantageous production method. Thus, the purpose of the present invention is
An object of the present invention is to provide a method for producing 3-chloro-1-thiocyanato-2-propene industrially easily and in a high yield.

【0004】[0004]

【課題を解決するための手段】本発明によれば、上記の
目的は、1,3−ジクロロプロペンとチオシアン酸塩
を、相間移動触媒の存在下に有機溶媒中で反応させるこ
とを特徴とする3−クロロ−1−チオシアナト−2−プ
ロペンの製造法を提供することにより達成される。
According to the present invention, the object is to react 1,3-dichloropropene with thiocyanate in an organic solvent in the presence of a phase transfer catalyst. This is achieved by providing a process for producing 3-chloro-1-thiocyanato-2-propene.

【0005】[0005]

【発明の実施の形態】本発明の反応に使用されるチオシ
アン酸塩としては、例えばチオシアン酸ナトリウム、チ
オシアン酸カリウム等のアルカリ金属塩;チオシアン酸
カルシウム、チオシアン酸マグネシウム等のアルカリ土
類金属塩;チオシアン酸アンモニウム塩等が挙げられ
る。中でも、チオシアン酸ナトリウムを使用するのが好
ましい。チオシアン酸塩の使用量は、1,3−ジクロロ
プロペン1モルに対して1.0〜1.5モルの範囲が好
ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The thiocyanate used in the reaction of the present invention includes, for example, alkali metal salts such as sodium thiocyanate and potassium thiocyanate; alkaline earth metal salts such as calcium thiocyanate and magnesium thiocyanate; And ammonium thiocyanate. Among them, it is preferable to use sodium thiocyanate. The use amount of the thiocyanate is preferably in the range of 1.0 to 1.5 mol per 1 mol of 1,3-dichloropropene.

【0006】本発明において使用される有機溶媒は、反
応に悪影響を与えない限り特に制限されないが、例えば
ベンゼン、トルエン、ヘキサン、ヘプタン、オクタン等
の炭化水素;ジクロロメタン、クロロホルム、四塩化炭
素、1,2−ジクロロエタン、1,1,2,2−テトラ
クロロエタン等のハロゲン化炭化水素;ジエチルエーテ
ル、ジイソプロピルエーテル、ジメトキシエタン、テト
ラヒドロフラン等のエーテル;アセトン、メチルエチル
ケトン、シクロヘキサノン等のケトン;アセトニトリ
ル、プロピオニトリル等のニトリル;メタノール、エタ
ノール、プロパノール等のアルコール;ジメチルスルホ
キシド等が挙げられる。有機溶媒の使用量はチオシアン
酸塩に対して0.5〜10重量倍が好ましく、1.0〜
2.0重量倍がより好ましい。
The organic solvent used in the present invention is not particularly limited as long as it does not adversely affect the reaction. For example, hydrocarbons such as benzene, toluene, hexane, heptane and octane; dichloromethane, chloroform, carbon tetrachloride, 1,4 Halogenated hydrocarbons such as 2-dichloroethane and 1,1,2,2-tetrachloroethane; ethers such as diethyl ether, diisopropyl ether, dimethoxyethane and tetrahydrofuran; ketones such as acetone, methyl ethyl ketone and cyclohexanone; acetonitrile, propionitrile and the like Nitrile; alcohols such as methanol, ethanol, and propanol; and dimethyl sulfoxide. The amount of the organic solvent used is preferably 0.5 to 10 times by weight of the thiocyanate, and
2.0 times by weight is more preferable.

【0007】また反応基質である1,3−ジクロロプロ
ペンを過剰に用いることにより、該反応基質に溶媒とし
ての役割を兼ねさせることもできる。
Further, by using an excess of 1,3-dichloropropene as a reaction substrate, the reaction substrate can also serve as a solvent.

【0008】本発明における反応は相間移動触媒の存在
下に行う。相間移動触媒を使用することにより、高収率
で3−クロロ−1−チオシアナト−2−プロペンを製造
することができる。例えば、溶媒としてジメチルスルホ
キシドを用いた場合、相間移動触媒を使用しないと収率
47%であるのに対し、相間移動触媒を使用すると収率
が70%にまで向上する(前述のJournal f. prakt. Ch
emie. Band 322, Heft4, 1980, S, 629および後述の実
施例3参照)。また、ジイソプロピルエーテルの場合、
相間移動触媒を使用しないとほとんど反応が進行しない
のに対し、相間移動触媒を使用すると収率が82%にま
で向上する(後述の実施例1および比較例1参照)。
The reaction in the present invention is carried out in the presence of a phase transfer catalyst. By using a phase transfer catalyst, 3-chloro-1-thiocyanato-2-propene can be produced in high yield. For example, when dimethyl sulfoxide is used as a solvent, the yield is 47% without using a phase transfer catalyst, whereas the yield is improved to 70% when a phase transfer catalyst is used (see the above-mentioned Journal f. Prakt). . Ch
emie. Band 322, Heft4, 1980, S, 629 and Example 3 described later). In the case of diisopropyl ether,
The reaction hardly proceeds without the use of a phase transfer catalyst, whereas the use of a phase transfer catalyst improves the yield to 82% (see Example 1 and Comparative Example 1 described later).

【0009】相間移動触媒としては、4級アンモニウム
塩、4級ホスホニウム塩、なかでもテトラメチルアンモ
ニウムクロリド、テトラエチルアンモニウムクロリド、
テトラブチルアンモニウムクロリド、ベンジルトリメチ
ルアンモニウムクロリドが好ましい。相間移動触媒の使
用量は、通常1,3−ジクロロプロペン1モルに対して
0.001〜0.01モルの範囲が適当である。
As the phase transfer catalyst, quaternary ammonium salts, quaternary phosphonium salts, especially tetramethylammonium chloride, tetraethylammonium chloride,
Tetrabutylammonium chloride and benzyltrimethylammonium chloride are preferred. The amount of the phase transfer catalyst to be used is usually in the range of 0.001 to 0.01 mol per 1 mol of 1,3-dichloropropene.

【0010】反応温度は0〜150℃の範囲が好まし
く、20〜80℃の範囲がより好ましい。反応時間は、
反応条件によっても異なるが、通常1〜4時間が適当で
ある。
[0010] The reaction temperature is preferably in the range of 0 to 150 ° C, more preferably in the range of 20 to 80 ° C. The reaction time is
Although it depends on the reaction conditions, it is usually appropriate for 1 to 4 hours.

【0011】このようにして得られた3−クロロ−1−
チオシアナト−2−プロペンの反応混合物からの単離・
精製は常法にしたがって行う。例えば、反応混合物を冷
却したのち、トルエン、ジエチルエーテル、塩化メチレ
ン、酢酸エチル等の有機溶媒で抽出し、抽出液を飽和食
塩水で洗浄したのち乾燥し、減圧下に濃縮し、濃縮物を
減圧蒸留、クロマトグラフィー等で分離精製することに
より行う。
[0011] The thus obtained 3-chloro-1-
Isolation of thiocyanato-2-propene from reaction mixture
Purification is performed according to a conventional method. For example, after cooling the reaction mixture, the mixture is extracted with an organic solvent such as toluene, diethyl ether, methylene chloride, and ethyl acetate.The extract is washed with saturated saline, dried, concentrated under reduced pressure, and the concentrate is concentrated under reduced pressure. The separation and purification are performed by distillation, chromatography and the like.

【0012】原料となる1,3−ジクロロプロペンは殺
線虫剤として大量生産されており、安価に容易に入手可
能である。
1,3-Dichloropropene as a raw material is mass-produced as a nematicide and is easily available at low cost.

【0013】本発明により製造される3−クロロ−1−
チオシアナト−2−プロペンは、銅塩等の金属塩の存在
下に転位させ、得られた3−クロロ−1−イソチオシア
ナト−1−プロペンに塩素化剤を作用させることにより
2−クロロ−5−クロロメチル−1,3−チアゾールに
変換することができる。2−クロロ−5−クロロメチル
−1,3−チアゾールは、例えば殺虫剤として有用なヘ
キサヒドロトリアジン化合物の合成中間体として有用で
ある(特公平6−776号公報参照)。
3-Chloro-1- produced according to the present invention
Thiocyanato-2-propene is rearranged in the presence of a metal salt such as a copper salt, and the obtained 3-chloro-1-isothiocyanato-1-propene is allowed to react with a chlorinating agent to give 2-chloro-5-chlorobenzene. It can be converted to methyl-1,3-thiazole. 2-Chloro-5-chloromethyl-1,3-thiazole is useful, for example, as a synthetic intermediate of a hexahydrotriazine compound useful as an insecticide (see Japanese Patent Publication No. 6-776).

【0014】[0014]

【実施例】以下、実施例等により本発明をさらに具体的
に説明するが、本発明はこれらの実施例により何ら限定
されるものではない。
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to Examples and the like, but the present invention is not limited to these Examples.

【0015】実施例1 ジイソプロピルエーテル12mlに、チオシアン酸ナト
リウム2.14g、1,3−ジクロロプロペン2.66
gおよびテトラエチルアンモニウムクロライド33mg
を加え、ジイソプロピルエーテルが還流する温度(68
〜70℃)で3時間加熱した。反応混合物を室温まで冷
却し、析出した塩類を濾過した。濾液を飽和食塩水20
mlで洗浄し、無水硫酸ナトリウム上で乾燥し、減圧下
に濃縮した。次に、濃縮物を減圧蒸留により精製し、3
−クロロ−1−チオシアナト−2−プロペン2.71g
を得た。 収率:82.7% 純度:97.9% 沸点:83〜88℃/5mmHg1 NMR−スペクトル(CDCl3 )δ:6.42(d,J=7.0H
z,(cis)), 6.39(d,J=14.0Hz,(trans)), 6.06(dt,J=14.
0,7.8Hz,(trans)), 6.04(dt,J=7.0,7.0Hz,(cis)), 3.80
(d,J=7.0Hz,(cis)), 3.59(d,J=7.8Hz,(trans))
Example 1 In 12 ml of diisopropyl ether, 2.14 g of sodium thiocyanate and 2.66 of 1,3-dichloropropene were used.
g and tetraethylammonium chloride 33mg
And the temperature at which diisopropyl ether refluxes (68
(-70 ° C) for 3 hours. The reaction mixture was cooled to room temperature, and the precipitated salts were filtered. The filtrate was washed with saturated saline 20
Washed with ml, dried over anhydrous sodium sulfate and concentrated under reduced pressure. Next, the concentrate was purified by distillation under reduced pressure,
2.71 g of -chloro-1-thiocyanato-2-propene
I got Yield: 82.7% Purity: 97.9% boiling point: 83~88 ℃ / 5mmHg 1 NMR- spectrum (CDCl 3) δ: 6.42 ( d, J = 7.0H
z, (cis)), 6.39 (d, J = 14.0Hz, (trans)), 6.06 (dt, J = 14.
0,7.8Hz, (trans)), 6.04 (dt, J = 7.0,7.0Hz, (cis)), 3.80
(d, J = 7.0Hz, (cis)), 3.59 (d, J = 7.8Hz, (trans))

【0016】実施例2 トルエン20mlに、チオシアン酸ナトリウム2.14
g、1,3−ジクロロプロペン2.66gおよびテトラ
ブチルアンモニウムクロライド43mgを加え、トルエ
ンが還流する温度(80〜85℃)で5時間加熱した。
反応混合物を室温まで冷却し、水20mlを加えて塩類
を溶解させた。有機層を分離し、飽和食塩水20mlで
洗浄したのち、無水硫酸ナトリウム上で乾燥し、減圧下
に濃縮した。次に、濃縮物を減圧蒸留により精製し、3
−クロロ−1−チオシアナト−2−プロペン2.59g
を得た。 収率:78.6% 純度:97.4%
Example 2 To 20 ml of toluene was added 2.14 sodium thiocyanate.
g, 2.66 g of 1,3-dichloropropene and 43 mg of tetrabutylammonium chloride were added, and the mixture was heated at a temperature at which toluene refluxed (80 to 85 ° C.) for 5 hours.
The reaction mixture was cooled to room temperature, and 20 ml of water was added to dissolve the salts. The organic layer was separated, washed with 20 ml of saturated saline, dried over anhydrous sodium sulfate, and concentrated under reduced pressure. Next, the concentrate was purified by distillation under reduced pressure,
-Chloro-1-thiocyanato-2-propene 2.59 g
I got Yield: 78.6% Purity: 97.4%

【0017】実施例3 ジメチルスルホキシド20mlに、チオシアン酸ナトリ
ウム2.14g、1,3−ジクロロプロペン2.66g
およびテトラブチルアンモニウムクロライド43mgを
加え、25〜30℃で3時間反応させた。反応混合物に
水100mlおよびイソプロピルエーテル100mlを
加えて攪拌、静置させ、有機層を分離し、飽和食塩水5
0mlで洗浄したのち、無水硫酸ナトリウム上で乾燥
し、減圧下に濃縮した。次に減圧蒸留により精製し、3
−クロロ−1−チオシアナト−2−プロペン2.41g
を得た。 収率:73.0% 純度:97.2%
Example 3 In 20 ml of dimethyl sulfoxide, 2.14 g of sodium thiocyanate and 2.66 g of 1,3-dichloropropene were used.
And 43 mg of tetrabutylammonium chloride, and the mixture was reacted at 25 to 30 ° C. for 3 hours. 100 ml of water and 100 ml of isopropyl ether were added to the reaction mixture, and the mixture was stirred and allowed to stand, and the organic layer was separated.
After washing with 0 ml, it was dried over anhydrous sodium sulfate and concentrated under reduced pressure. Next, the product is purified by distillation under reduced pressure.
-Chloro-1-thiocyanato-2-propene 2.41 g
I got Yield: 73.0% Purity: 97.2%

【0018】比較例1 ジイソプロピルエーテル12mlに、チオシアン酸ナト
リウム2.14gおよび1,3−ジクロロプロペン2.
66gを加え、ジイソプロピルエーテルが還流する温度
(68〜70℃)で7時間反応させたが、ほとんど反応
が進行せず、目的とする3−クロロ−1−チオシアナト
−2−プロペン2.71gは痕跡量しか得られなかっ
た。
Comparative Example 1 2.14 g of sodium thiocyanate and 1,3-dichloropropene in 12 ml of diisopropyl ether
66 g was added, and the mixture was reacted at a temperature at which diisopropyl ether was refluxed (68 to 70 ° C.) for 7 hours. Only the amount was obtained.

【0019】[0019]

【発明の効果】本発明によれば、1−チオシアナト−3
−クロロ−2−プロペンを高収率で工業的に有利に製造
することができる。
According to the present invention, 1-thiocyanato-3
-Chloro-2-propene can be industrially advantageously produced in high yield.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 1,3−ジクロロプロペンとチオシアン
酸塩を、相間移動触媒の存在下に有機溶媒中で反応させ
ることを特徴とする3−クロロ−1−チオシアナト−2
−プロペンの製造法。
1. A reaction between 1,3-dichloropropene and thiocyanate in an organic solvent in the presence of a phase transfer catalyst in 3-chloro-1-thiocyanato-2.
-A process for producing propene.
JP8207046A 1996-02-21 1996-08-06 Production of 3-chloro-1-thiocyanate-2-propene Pending JPH1045710A (en)

Priority Applications (11)

Application Number Priority Date Filing Date Title
JP8207046A JPH1045710A (en) 1996-08-06 1996-08-06 Production of 3-chloro-1-thiocyanate-2-propene
IN276CA1997 IN182219B (en) 1996-02-21 1997-02-17
EP97102811A EP0794180B1 (en) 1996-02-21 1997-02-20 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole
AT97102811T ATE228509T1 (en) 1996-02-21 1997-02-20 METHOD FOR PRODUCING 2-CHLORO-5-CHLOROMETHYL-1,3-THIAZOLE
DE69717330T DE69717330T2 (en) 1996-02-21 1997-02-20 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole
AU14819/97A AU690866B2 (en) 1996-02-21 1997-02-20 Process for the preparation of 2-chloro-5-chloromethyl-1, 3-thiazole
CN97109983A CN1073096C (en) 1996-02-21 1997-02-21 Process for preparation of 2 -chloro -5 -cholromethyl -1, 3 -thiazole
US08/804,401 US5894073A (en) 1996-02-21 1997-02-21 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole
US09/225,292 US6103921A (en) 1996-02-21 1999-01-05 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole
US09/545,349 US6222057B1 (en) 1996-02-21 2000-04-07 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole
US09/547,221 US6245927B1 (en) 1996-02-21 2000-04-11 Process for the preparation of 2-chloro-5-chloromethyl-1,3-thiazole

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8207046A JPH1045710A (en) 1996-08-06 1996-08-06 Production of 3-chloro-1-thiocyanate-2-propene

Publications (1)

Publication Number Publication Date
JPH1045710A true JPH1045710A (en) 1998-02-17

Family

ID=16533316

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8207046A Pending JPH1045710A (en) 1996-02-21 1996-08-06 Production of 3-chloro-1-thiocyanate-2-propene

Country Status (1)

Country Link
JP (1) JPH1045710A (en)

Cited By (1)

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Publication number Priority date Publication date Assignee Title
CN114539114A (en) * 2022-02-26 2022-05-27 河北野田农用化学有限公司 Continuous production process and reactor for iso-ester

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114539114A (en) * 2022-02-26 2022-05-27 河北野田农用化学有限公司 Continuous production process and reactor for iso-ester
CN114539114B (en) * 2022-02-26 2023-11-24 河北野田农用化学有限公司 Continuous production process and reactor for isoaster

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