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JPH10167999A - Method for producing bromomethylcyclopropane - Google Patents

Method for producing bromomethylcyclopropane

Info

Publication number
JPH10167999A
JPH10167999A JP33175396A JP33175396A JPH10167999A JP H10167999 A JPH10167999 A JP H10167999A JP 33175396 A JP33175396 A JP 33175396A JP 33175396 A JP33175396 A JP 33175396A JP H10167999 A JPH10167999 A JP H10167999A
Authority
JP
Japan
Prior art keywords
bromomethylcyclopropane
bromine
cyclopropanemethanol
complex
producing
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
JP33175396A
Other languages
Japanese (ja)
Inventor
Tatsuhiko Hayashibara
太津彦 林原
Toshimichi Mitani
利道 三谷
Manzo Shiono
万蔵 塩野
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 JP33175396A priority Critical patent/JPH10167999A/en
Publication of JPH10167999A publication Critical patent/JPH10167999A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C17/00Preparation of halogenated hydrocarbons
    • C07C17/093Preparation of halogenated hydrocarbons by replacement by halogens
    • C07C17/16Preparation of halogenated hydrocarbons by replacement by halogens of hydroxyl groups

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

(57)【要約】 【課題】 不純物の少ないブロモメチルシクロプロパン
を、高い選択性を保持し、工業的に有利に製造する方法
を提供する。 【解決手段】 シクロプロパンメタノールを、炭化水素
溶媒中、0℃〜40℃の温度で、ジメチルスルフィドと
臭素の錯体にて臭素化したのち、脱臭処理を行うことを
特徴とするブロモメチルシクロプロパンの製造方法。
PROBLEM TO BE SOLVED: To provide a method for industrially advantageously producing bromomethylcyclopropane having a small amount of impurities while maintaining high selectivity. SOLUTION: Bromomethyl cyclopropane is obtained by brominating cyclopropanemethanol in a hydrocarbon solvent at a temperature of 0 ° C to 40 ° C with a complex of dimethylsulfide and bromine, and then performing a deodorizing treatment. Production method.

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】本発明は医薬品原料として有
用なブロモメチルシクロプロパンの製造方法に関するも
のである。
The present invention relates to a method for producing bromomethylcyclopropane, which is useful as a raw material for pharmaceuticals.

【0002】[0002]

【従来の技術】ブロモメチルシクロプロパンの製造方法
として、シクロプロパンメタノールに三臭化リンを作用
させる方法が知られているが[J. Am. Chem. Soc. 、2
509頁(1951年)参照]、この方法では副生成物
であるシクロブチルブロマイドが20%、4−ブロモ−
1−ブテンが6%生成する。そこで、このようなシクロ
プロパン環が開裂した副生成物の生成を抑制するため
に、三臭化リンの調製を−80℃の低温で行う方法が知
られている[J. Am. Chem. Soc. 、6675頁(195
5年)参照]。また、ブロム化剤としてトリフェニルホ
スフィン−四臭化炭素を使用する方法も知られている
[J. Org. Chem. 、49巻、431頁(1984年)参
照]。また、シクロプロパンメタノールを臭素−ジメチ
ルスルフィド錯体にてブロム化する方法も知られている
[J. C. S. Chem. Comm.、212頁(1973年)]。
2. Description of the Related Art As a method for producing bromomethylcyclopropane, a method of reacting phosphorus tribromide with cyclopropanemethanol is known [J. Am. Chem. Soc.
509 (1951)]. In this method, by-product cyclobutyl bromide is 20%, 4-bromo-
6% of 1-butene is formed. Therefore, in order to suppress the formation of such a by-product in which the cyclopropane ring is cleaved, there is known a method of preparing phosphorus tribromide at a low temperature of -80 ° C [J. Am. Chem. , P. 6675 (195
5)). Also, a method using triphenylphosphine-carbon tetrabromide as a brominating agent is known [see J. Org. Chem., 49, 431 (1984)]. A method of brominating cyclopropanemethanol with a bromine-dimethylsulfide complex is also known [JCS Chem. Comm., P. 212 (1973)].

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記の
三臭化リンまたはトリフェニルホスフィン−四臭化炭素
をブロム化剤として使用する方法では、これらのブロム
化剤が高価である上、大量のリン廃棄物が副生する。ま
た、臭素−ジメチルスルフィド錯体を用いる方法につい
ては、得られるブロモメチルシクロプロパンの純度は記
載されていない。また、臭素−ジメチルスルフィド錯体
を予め別途調製、単離して用いていることから、操作が
繁雑な上、原料のシクロプロパンメタノールを大過剰に
用いる必要があり、反応後の精製も繁雑である。さらに
ジメチルスルフィドに由来する悪臭が通常の蒸留だけで
は除去できないため、該方法は工業的に実施する上で問
題点を有していた。しかして、本発明の目的は、不純物
の少ないブロモメチルシクロプロパンを、高い選択性を
保持し、工業的に有利に製造する方法を提供することに
ある。
However, in the above-mentioned method using phosphorus tribromide or triphenylphosphine-carbon tetrabromide as a brominating agent, these brominating agents are expensive and a large amount of phosphorus is used. Waste is by-produced. Further, regarding the method using a bromine-dimethyl sulfide complex, the purity of the obtained bromomethylcyclopropane is not described. Further, since the bromine-dimethylsulfide complex is separately prepared, isolated and used in advance, the operation is complicated, and it is necessary to use a large excess of the starting material cyclopropanemethanol, and the purification after the reaction is also complicated. Furthermore, since the odor derived from dimethyl sulfide cannot be removed only by ordinary distillation, the method has a problem in industrially implementing the method. Accordingly, an object of the present invention is to provide a method for industrially advantageously producing bromomethylcyclopropane containing few impurities while maintaining high selectivity.

【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、シクロプロパンメタノールを、炭化水素溶媒
中、0℃〜40℃の温度で、ジメチルスルフィドと臭素
の錯体にて臭素化したのち、脱臭処理を行うことを特徴
とするブロモメチルシクロプロパンの製造方法を提供す
ることにより達成される。
According to the present invention, the above object is achieved by brominating cyclopropanemethanol with a complex of dimethylsulfide and bromine in a hydrocarbon solvent at a temperature of 0 ° C to 40 ° C. Thereafter, a deodorizing treatment is performed, which is achieved by providing a method for producing bromomethylcyclopropane.

【0005】[0005]

【発明の実施の形態】ジメチルスルフィドと臭素の錯体
は固体のため、シクロプロパンメタノール基準の収率を
上げるためには希釈剤が必要であり、希釈剤としては、
炭化水素溶媒が使用される。炭化水素溶媒としては、ペ
ンタン、ヘキサン、2−メチルブタン、オクタン、シク
ロペンタン、シクロヘキサンなどの直鎖状、分岐状また
は環状の炭化水素が用いられる。特にペンタン、ヘキサ
ンなどが好ましい。炭化水素溶媒以外の溶媒では反応の
選択率が低下する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Since a complex of dimethyl sulfide and bromine is a solid, a diluent is required to increase the yield based on cyclopropanemethanol.
Hydrocarbon solvents are used. As the hydrocarbon solvent, a linear, branched or cyclic hydrocarbon such as pentane, hexane, 2-methylbutane, octane, cyclopentane and cyclohexane is used. Particularly, pentane, hexane and the like are preferable. Solvents other than hydrocarbon solvents reduce the selectivity of the reaction.

【0006】ジメチルスルフィドの使用量は、シクロプ
ロパンメタノール1モルに対し、0.4〜1.0モルの
範囲の量が好ましい。また、臭素の使用量は、シクロプ
ロパンメタノール1モルに対し、0.4〜1.0モルの
範囲の量が好ましく、0.5〜0.8モルの範囲の量が
経済性の面からより好ましい。ジメチルスルフィドと臭
素の錯体はシクロプロパンメタノールの添加に先立ち、
上記溶媒中で冷却下にジメチルスルフィドと臭素を反応
させることにより調製され、単離することなくその懸濁
液のままシクロプロパンメタノールとの反応に供するこ
とができる。
The amount of dimethyl sulfide used is preferably in the range of 0.4 to 1.0 mol based on 1 mol of cyclopropanemethanol. The amount of bromine used is preferably in the range of 0.4 to 1.0 mol per mol of cyclopropane methanol, and more preferably in the range of 0.5 to 0.8 mol in terms of economy. preferable. The complex of dimethyl sulfide and bromine, prior to the addition of cyclopropanemethanol,
It is prepared by reacting dimethyl sulfide with bromine under cooling in the above-mentioned solvent, and can be subjected to a reaction with cyclopropane methanol as a suspension without isolation.

【0007】反応は、0℃〜40℃の範囲の温度で行う
が、20℃〜40℃の範囲の温度がより好ましい。40
℃より高い温度ではシクロプロパン環が開環しやすくな
るため、好ましくない。
[0007] The reaction is carried out at a temperature in the range of 0 ° C to 40 ° C, more preferably in the range of 20 ° C to 40 ° C. 40
If the temperature is higher than 0 ° C., the cyclopropane ring tends to open, which is not preferable.

【0008】ブロム化反応終了後、反応液からの目的物
の単離精製は、相分離している下層を除去した後、洗
浄、蒸留することにより行うことができるが、ジメチル
スルフィド由来の臭気が伴うため、蒸留前あるいは蒸留
後に脱臭を行う必要がある。
After the completion of the bromination reaction, the desired product can be isolated and purified from the reaction solution by removing the lower layer in which phase separation has occurred, followed by washing and distillation, but the odor derived from dimethyl sulfide is eliminated. Therefore, it is necessary to deodorize before or after distillation.

【0009】脱臭操作としては、過酸化水素水との接
触、活性炭による吸着などの方法が用いられる。過酸化
水素水としては、含有するジメチルスルフィドに対し、
2〜20モル当量の過酸化水素を含有する5〜35%濃
度の水溶液が用いられ、−5〜10℃の温度にてブロモ
メチルシクロプロパンまたはその溶液と0.5〜10時
間接触させることにより脱臭が完了する。また、活性炭
はその吸着力により使用量が異なるが0〜70℃でジメ
チルスルフィドが消失するまで添加し、その後濾過する
ことにより脱臭が完了する。
As the deodorizing operation, methods such as contact with hydrogen peroxide solution and adsorption with activated carbon are used. As the aqueous hydrogen peroxide, for the dimethyl sulfide contained,
A 5-35% strength aqueous solution containing 2-20 molar equivalents of hydrogen peroxide is used and is contacted with bromomethylcyclopropane or a solution thereof for 0.5-10 hours at a temperature of -5-10 ° C. Deodorization is completed. Activated carbon is used in different amounts depending on its adsorptive power, but is added at 0 to 70 ° C. until dimethyl sulfide disappears, and then filtered to complete deodorization.

【0010】[0010]

【実施例】以下、実施例により本発明をさらに詳しく説
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 The present invention will be described in more detail with reference to the following Examples, which should not be construed as limiting the present invention.

【0011】実施例1 窒素雰囲気下、ジメチルスルフィド37.3gを溶解し
たヘキサン600mlの溶液に、氷冷下、臭素95.9
gを2時間かけて滴下し、さらに1時間撹拌してジメチ
ルスルフィド−臭素錯体の懸濁液を調製した。この懸濁
液に、25℃にてシクロプロパンメタノール72.1g
を2時間で滴下し、25〜30℃にて一夜攪拌を続け
た。得られた反応液を分液して下層を除去し、上層に0
℃にて10%過酸化水素水500mlを2時間かけて滴
下し、0℃で3時間攪拌を続けた。水層を除去し上層を
重曹水で洗浄したのち、ヘキサンを留去し、減圧下に蒸
留することにより、ブロモメチルシクロプロパンを10
1.3g得た(収率75%)。
Example 1 95.9 bromine was added to a solution of 37.3 g of dimethyl sulfide in 600 ml of hexane under a nitrogen atmosphere under ice-cooling.
g was added dropwise over 2 hours and further stirred for 1 hour to prepare a suspension of dimethylsulfide-bromine complex. 72.1 g of cyclopropanemethanol was added to this suspension at 25 ° C.
Was added dropwise over 2 hours, and stirring was continued at 25 to 30 ° C. overnight. The resulting reaction mixture was separated to remove the lower layer, and the upper layer was
500 ml of 10% hydrogen peroxide solution was added dropwise at 2 ° C. over 2 hours, and stirring was continued at 0 ° C. for 3 hours. After removing the aqueous layer and washing the upper layer with aqueous sodium bicarbonate, hexane was distilled off and distilled under reduced pressure to remove bromomethylcyclopropane.
1.3 g was obtained (yield 75%).

【0012】実施例2 実施例1と同様に調製した反応液の下層を除去し上層を
重曹水で洗浄した後、ヘキサンの約1/2を留去した。
残液に活性炭を10g加え、4時間撹拌したのち濾過
し、さらに濃縮したのち、減圧下に蒸留することによ
り、ブロモメチルシクロプロパンを87.7g得た(収
率65%)。
Example 2 The lower layer of the reaction solution prepared in the same manner as in Example 1 was removed, and the upper layer was washed with aqueous sodium bicarbonate, and about の of hexane was distilled off.
Activated carbon (10 g) was added to the residue, and the mixture was stirred for 4 hours, filtered, concentrated, and distilled under reduced pressure to obtain bromomethylcyclopropane (87.7 g, yield 65%).

【0013】[0013]

【発明の効果】不純物の少ないブロモメチルシクロプロ
パンを、高い選択性を保持し、工業的に有利に製造する
方法が提供される。
According to the present invention, there is provided a method for industrially advantageously producing bromomethylcyclopropane containing few impurities while maintaining high selectivity.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 シクロプロパンメタノールを、炭化水素
溶媒中、0℃〜40℃の温度で、ジメチルスルフィドと
臭素の錯体にて臭素化したのち、脱臭処理を行うことを
特徴とするブロモメチルシクロプロパンの製造方法。
1. Bromomethylcyclopropane, which is obtained by brominating cyclopropanemethanol with a complex of dimethylsulfide and bromine in a hydrocarbon solvent at a temperature of 0 ° C. to 40 ° C. and then performing a deodorizing treatment. Manufacturing method.
【請求項2】 ジメチルスルフィドと臭素の錯体をシク
ロプロパンメタノール1モルに対して0.4〜1.0モ
ル使用する請求項1記載の製造方法。
2. The process according to claim 1, wherein the complex of dimethyl sulfide and bromine is used in an amount of 0.4 to 1.0 mol per 1 mol of cyclopropanemethanol.
JP33175396A 1996-12-12 1996-12-12 Method for producing bromomethylcyclopropane Pending JPH10167999A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33175396A JPH10167999A (en) 1996-12-12 1996-12-12 Method for producing bromomethylcyclopropane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33175396A JPH10167999A (en) 1996-12-12 1996-12-12 Method for producing bromomethylcyclopropane

Publications (1)

Publication Number Publication Date
JPH10167999A true JPH10167999A (en) 1998-06-23

Family

ID=18247240

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33175396A Pending JPH10167999A (en) 1996-12-12 1996-12-12 Method for producing bromomethylcyclopropane

Country Status (1)

Country Link
JP (1) JPH10167999A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6077981A (en) * 1998-08-28 2000-06-20 Eastman Chemical Company Process for the production of cyclopropylmethyl halides
WO2001009068A3 (en) * 1999-08-03 2001-03-22 Eastman Chem Co Process for the production of cyclopropylmethyl halides

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6077981A (en) * 1998-08-28 2000-06-20 Eastman Chemical Company Process for the production of cyclopropylmethyl halides
WO2001009068A3 (en) * 1999-08-03 2001-03-22 Eastman Chem Co Process for the production of cyclopropylmethyl halides

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