JPH0710829B2 - Method for producing benzyl mercaptan derivative - Google Patents
Method for producing benzyl mercaptan derivativeInfo
- Publication number
- JPH0710829B2 JPH0710829B2 JP61137852A JP13785286A JPH0710829B2 JP H0710829 B2 JPH0710829 B2 JP H0710829B2 JP 61137852 A JP61137852 A JP 61137852A JP 13785286 A JP13785286 A JP 13785286A JP H0710829 B2 JPH0710829 B2 JP H0710829B2
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- Prior art keywords
- group
- carbon atoms
- alkyl group
- halogen atom
- producing
- Prior art date
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Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、ベンジルメルカプタン誘導体の新規な製造法
に関する。本発明のベンジルメルカプタン誘導体は、農
薬、特に殺虫、殺ダニ、殺線虫および殺菌剤の有効成分
化合物の中間体として有用である。TECHNICAL FIELD The present invention relates to a novel process for producing a benzylmercaptan derivative. INDUSTRIAL APPLICABILITY The benzyl mercaptan derivative of the present invention is useful as an intermediate of active ingredient compounds of agricultural chemicals, especially insecticides, acaricides, nematicides and fungicides.
〔従来の技術〕 ベンジルメルカプタン誘導体の製造法としては、米国特
許第2,456,588号公報に、ベンジルクロライドと水硫化
ソーダとを、水を溶媒として用いて、反応させて、ベン
ジルメルカプタンを得る方法が記載されている。しか
し、本発明者らは、この方法について、追試を行ったと
ころ、収率は約30%程度であった。(Prior Art) As a method for producing a benzyl mercaptan derivative, U.S. Pat.No. 2,456,588 describes a method of obtaining benzyl mercaptan by reacting benzyl chloride and sodium hydrosulfide with water as a solvent. ing. However, the inventors of the present invention conducted additional tests on this method and found that the yield was about 30%.
一方、この方法において、ハイドロキノン,青酸カリウ
ム,ビス(2−クロロエチル)エーテル,グリセロール
等を添加すると、収率向上の効果がある旨、記載されて
いるので、本発明者は、本発明の製造法に、上記物質を
添加して行ったところ、添加しない場合に比べて、むし
ろ収率が低下することが判かった。On the other hand, in this method, it is described that the addition of hydroquinone, potassium cyanide, bis (2-chloroethyl) ether, glycerol, etc. has the effect of improving the yield. In addition, when the above substances were added, it was found that the yield was rather reduced as compared with the case where the above substances were not added.
ベンジルメルカプタン誘導体の工業的に有利な製造法が
要望され、特に、高収率で得る方法が要望されている。There is a demand for an industrially advantageous method for producing a benzyl mercaptan derivative, and in particular, a method for obtaining it in a high yield.
本発明は、ベンジルメルカプタン誘導体の新規な製造法
に関するものであり、更に詳しくは、本発明は、 次式(I): で表されるベンジルメルカプタン誘導体の製造法におい
て、 次式(II): で表されるベンジルハライド誘導体と、水硫化アルカリ
とを、水と非水溶性有機溶媒との混合溶媒中で、相間移
動触媒の存在下、反応させることを特徴とするベンジル
メルカプタン誘導体の製造法(以下A法という。)およ
び前記式(II)で表されるベンジルハライド誘導体と、
水硫化アルカリとを水溶性有機溶媒中で反応させること
を特徴とするベンジルメルカプタン誘導体の製造法(以
下、B法という。)並びに、A法もしくはB法のの際
に、特定の酸触媒を添加させることを特徴とするベンジ
ルメルカプタン誘導体の製造法に関するものである。The present invention relates to a novel method for producing a benzylmercaptan derivative, and more specifically, the present invention relates to the following formula (I): In the method for producing a benzyl mercaptan derivative represented by the following formula (II): A method for producing a benzyl mercaptan derivative, which comprises reacting a benzyl halide derivative represented by and an alkali hydrosulfide in a mixed solvent of water and a water-insoluble organic solvent in the presence of a phase transfer catalyst ( Hereinafter referred to as Method A) and a benzyl halide derivative represented by the above formula (II),
A method for producing a benzyl mercaptan derivative characterized by reacting with alkali hydrosulfide in a water-soluble organic solvent (hereinafter referred to as method B), and addition of a specific acid catalyst during method A or method B And a method for producing a benzyl mercaptan derivative.
〔上記式中、Zはハロゲン原子を示し、Rは水素原子ま
たは低級アルキル基を示し、Xは炭素数1〜6の直鎖も
しくは分岐を有するアルキル基,炭素数1〜6の直鎖も
しくは分岐を有するアルコキシ基,炭素数3〜6のアル
ケニルオキシ基,低級ハロアルキル基,炭素数3〜6の
シクロアルキル基,ハロゲン原子, (但し、Yはハロゲン原子,低級アルキル基もしくは低
級ハロアルキル基を、mは0または1〜3の整数を示
し、mが2または3の場合は、Yは同一でも互いに異な
ってもよい。)またはトリメチルシリル基を示し、n
は、1〜3の整数を示す。nが2または3の場合はXは
同一でも互いに異なってもよい。〕。[In the above formula, Z represents a halogen atom, R represents a hydrogen atom or a lower alkyl group, X represents a linear or branched alkyl group having 1 to 6 carbon atoms, a linear or branched alkyl group having 1 to 6 carbon atoms. An alkoxy group having 3 to 6 carbon atoms, an alkenyloxy group having 3 to 6 carbon atoms, a lower haloalkyl group, a cycloalkyl group having 3 to 6 carbon atoms, a halogen atom, (However, Y represents a halogen atom, a lower alkyl group or a lower haloalkyl group, m represents an integer of 0 or 1 to 3, and when m is 2 or 3, Y may be the same or different from each other.) Trimethylsilyl group, n
Represents an integer of 1 to 3. When n is 2 or 3, X may be the same or different from each other. ].
本発明の方法によれば、目的とするベンジルメルカプタ
ン誘導体の収率が少くとも70%以上、場合によっては、
90%以上の高収率で実施できる。次に本発明のA法およ
びB法について、具体的に説明する。According to the method of the present invention, the yield of the target benzyl mercaptan derivative is at least 70% or more, and in some cases,
It can be performed with a high yield of 90% or more. Next, the methods A and B of the present invention will be specifically described.
A法について 本発明者らが見出したA法を、反応式で示せば、次の通
りである。Method A The method A found by the present inventors is shown as a reaction formula as follows.
〔反応式中、Z,R,X,nは前記と同じ意味を表す。〕 上記反応式において、水硫化ソーダは、通常市販されて
いる固形の含水物又は水溶液のいずれも同様に使用する
ことができる。 [In the reaction formula, Z, R, X, and n have the same meanings as described above. In the above reaction formula, as the sodium hydrosulfide, any of commercially available solid hydrates or aqueous solutions can be similarly used.
非水溶性有機溶媒としては、ベンゼン,トルエン,キシ
レン等に代表される芳香族炭化水素類,ペンタン,ヘキ
サン,ヘプタン等に代表される脂肪族炭化水素類,ギ酸
エチルエステル,酢酸メチルエステル,酢酸エチルエス
テル等に代表されるエステル類,四塩化炭素,1,2-ジク
ロルエタン,メチルクロロホルム等に代表されるハロゲ
ン化炭化水素類,ジエチルエーテル,テトラヒドロフラ
ン,ジイソプロピルエーテル等に代表されるエーテル類
が挙げられる。これらの中でも特に好ましいのは芳香族
炭化水素類,エステル類,ハロゲン化炭化水素類であ
る。As the non-water-soluble organic solvent, aromatic hydrocarbons represented by benzene, toluene, xylene, etc., aliphatic hydrocarbons represented by pentane, hexane, heptane, ethyl formate, methyl acetate, ethyl acetate, etc. Examples thereof include esters such as esters, carbon tetrachloride, 1,2-dichloroethane, halogenated hydrocarbons such as methyl chloroform, and ethers such as diethyl ether, tetrahydrofuran, and diisopropyl ether. Among these, aromatic hydrocarbons, esters and halogenated hydrocarbons are particularly preferable.
相間移動触媒としては、テトラ−n−ブチルアンモニウ
ムブロマイド,テトラ−n−ブチルアンモニウムハイド
ロジェンスルフェイト,トリエチルベンジルアンモニウ
ムクロライド,テトラ−n−ブチルアンモニウムヒドロ
キサイド等に代表される第4級アンモニウム塩,テトラ
−n−ブチルホスホニウムブロマイド等に代表されるホ
スホニウム塩等が挙げられる。これらの中で特に好まし
いものは、テトラ−n−ブチルアンモニウムブロマイ
ド,テトラ−n−ブチルアンモニウムハイドロジェンス
ルフェイド等である。添加量は原料ベンジルハライド誘
導体に対し、0.1モル%以上、好ましくは0.5〜10モル%
に設定することが実用的である。As the phase transfer catalyst, a quaternary ammonium salt represented by tetra-n-butylammonium bromide, tetra-n-butylammonium hydrogensulfate, triethylbenzylammonium chloride, tetra-n-butylammonium hydroxide, tetra, etc. Examples include phosphonium salts represented by -n-butylphosphonium bromide. Among these, particularly preferred are tetra-n-butylammonium bromide, tetra-n-butylammonium hydrogensulfide and the like. The amount added is 0.1 mol% or more, preferably 0.5 to 10 mol%, based on the raw material benzyl halide derivative.
It is practical to set to.
反応温度は、0℃〜150℃付近で可能であるが、特には1
0℃〜100℃付近が好ましい。The reaction temperature can be around 0 ° C to 150 ° C, but especially 1
Around 0 ° C to 100 ° C is preferable.
更に、収率向上には上記製造法において、酸触媒を添加
することが好ましい。酸触媒としては、ギ酸,酢酸,プ
ロピオン酸,酪酸,蓚酸,酒石酸等に代表される脂肪酸
類,塩酸,硝酸,硫酸,リン酸,ホウ酸等に代表される
無機酸類,メタンスルホン酸,ベンゼンスルホン酸,P−
トルエンスルホン酸に代表されるスルホン酸類,硫酸ア
ンモニウム,硫酸水素アンモニウム,硝酸アンモニウム
等に代表される無機塩類等が挙げられ、特には脂肪族類
および無機酸類が優れている。添加量は原料ベンジルハ
ライド誘導体に対し、1モル%以上が好ましく、特には
5〜50モル%が実用的である。Further, in order to improve the yield, it is preferable to add an acid catalyst in the above production method. Examples of the acid catalyst include fatty acids such as formic acid, acetic acid, propionic acid, butyric acid, oxalic acid and tartaric acid, inorganic acids such as hydrochloric acid, nitric acid, sulfuric acid, phosphoric acid and boric acid, methanesulfonic acid and benzenesulfone. Acid, P-
Examples thereof include sulfonic acids typified by toluenesulfonic acid, inorganic salts typified by ammonium sulfate, ammonium hydrogen sulfate, ammonium nitrate, and the like, and aliphatics and inorganic acids are particularly excellent. The addition amount is preferably 1 mol% or more, and particularly 5 to 50 mol% is practical for the starting benzyl halide derivative.
B法について 本発明者らが見出したB法を、反応式で示せば次の通り
である。Method B The method B found by the present inventors is shown below by a reaction formula.
〔反応式中、Z,R,X,nは前記と同じ意味を表す。〕 上記反応式において、水硫化ソーダは、通常市販されて
いる固形の含水物又は、水溶液のいずれも同様に使用す
ることができるが、好ましくは、水溶液を用いるのがよ
い。 [In the reaction formula, Z, R, X, and n have the same meanings as described above. In the above reaction formula, sodium hydrosulfide can be used in the same manner as any of commercially available solid hydrates and aqueous solutions, but it is preferable to use an aqueous solution.
水溶性溶媒としては、メタノール,エタノール,プロパ
ノール等に代表される低級アルコール類,アセトン,メ
チルエチルケトン,ジイソブチルケトン等に代表される
ケトン類,アセトニトリル,プロピオニトリル等に代表
されるニトリル類,N,N-ジメチルホルムアミド,N,N-ジメ
チルアセトアミド等に代表されるアミド類,ジメチルス
ルホキシド,オキシラン等に代表されるオキシド類が挙
げられる。これらの中では、アルコール類,ケトン類,
ニトリル類のいずれもが優れた溶媒である。Examples of the water-soluble solvent include lower alcohols represented by methanol, ethanol, propanol, etc., ketones represented by acetone, methyl ethyl ketone, diisobutyl ketone, etc., nitriles represented by acetonitrile, propionitrile, etc., N, N -Amids such as dimethylformamide and N, N-dimethylacetamide, and oxides such as dimethyl sulfoxide and oxirane. Among these, alcohols, ketones,
All of the nitriles are excellent solvents.
このB法は均一反応であるので、反応の進行が速く、反
応温度は室温程度でも充分進行する。実用的には0℃〜
100℃付近が好ましい。Since this method B is a homogeneous reaction, the reaction proceeds rapidly, and the reaction temperature sufficiently proceeds even at room temperature. Practically 0 ℃ ~
Around 100 ° C is preferable.
B法も、A法と同様に酸触媒の添加による収率の向上が
みられる。使用できる酸触媒の種類としてはA法と同じ
である。In method B as well, as in method A, the yield is improved by adding an acid catalyst. The type of acid catalyst that can be used is the same as in Method A.
本発明方法によれば、従来法に比べて高収率で且つ容易
な操作で目的物を得ることができるという利点を有して
いる。The method of the present invention has an advantage that the target substance can be obtained with a high yield and an easy operation as compared with the conventional method.
次に本発明方法について実施例を具体的に挙げて説明す
る。Next, the method of the present invention will be described with reference to specific examples.
但し、本発明はこれらの実施例のみに限定されるもので
はない。However, the present invention is not limited to these examples.
実施例1 4−ターシャリーブチルベンジルメルカプタ
ンの製造 300ml四口反応フラスコにパラーターシャリーブチルベ
ンジルクロライド(以下TBCと略記する)18.3g(0.1モ
ル),トルエン100g,テトラブチルアンニモウムブロマ
イド0.5g,酢酸1.8g(0.03モル)を仕込み、50℃に加温
してから撹拌下に23%水硫化ソーダー水溶液31.7g(0.1
3モル)を30分で滴下した。Example 1 Preparation of 4-tert-butyl benzyl mercaptan Paratertiary butyl benzyl chloride (hereinafter abbreviated as TBC) 18.3 g (0.1 mol), toluene 100 g, tetrabutyl animonium bromide 0.5 g, in a 300 ml four-neck reaction flask. Charge 1.8 g (0.03 mol) of acetic acid, warm to 50 ° C, and then, with stirring, add 31.7 g (0.1%) of a 23% aqueous sodium hydrosulfide solution with stirring.
3 mol) was added dropwise in 30 minutes.
さらに30分50℃で撹拌を続け反応を完結させた。Stirring was continued for another 30 minutes at 50 ° C. to complete the reaction.
冷却し室温に戻してから分液し、トルエン層を水洗後、
濃縮することにより目的とする4−ターシャリーブチル
ベンジルメルカプタン(以下TBSHと略記する)の淡黄色
液体18.0g(純度93%),収率92%を得た。After cooling and returning to room temperature, liquid separation was performed, and the toluene layer was washed with water,
By concentrating, 18.0 g (purity 93%) of pale yellow liquid of the target 4-tert-butylbenzyl mercaptan (abbreviated as TBSH hereinafter) was obtained with a yield of 92%.
なお本実施例のスケールアップにより得られた粗TBSHを
蒸留することにより沸点90〜92℃/4mmHgの高純度(純度
99%)TBSHが得られた。In addition, by distilling the crude TBSH obtained by the scale-up of this example, a high purity (purity of 90 to 92 ° C / 4 mmHg (purity
99%) TBSH was obtained.
実施例2 4−ターシャリーブチルベンジルメルカプタ
ンの製造 300ml四口反応フラスコにTBC18.3g(0.1モル),トルエ
ン100g,テトラブチルアンニモウムブロマイド0.5gを仕
込み、50℃に加温してから撹拌下に23%水硫化ソーダー
水溶液31.7g(0.13モル)を30分で滴下した。さらに30
分50℃で撹拌を続け反応を完結させた。Example 2 Preparation of 4-tert-butyl benzyl mercaptan A 300 ml four-neck reaction flask was charged with 18.3 g (0.1 mol) of TBC, 100 g of toluene, and 0.5 g of tetrabutylanimium bromide, heated to 50 ° C., and then stirred. To the above, 31.7 g (0.13 mol) of 23% sodium hydrosulfide aqueous solution was added dropwise over 30 minutes. 30 more
The stirring was continued at 50 ° C. for 50 minutes to complete the reaction.
冷却し室温に戻してから分液し、得られたトルエン層を
水洗後、ガスクロマトグラフィーの内標分析法で定量し
た結果、目的とするTBSHの収率は71%であった。After cooling and returning to room temperature, the layers were separated, and the obtained toluene layer was washed with water and quantified by an internal standard analysis method of gas chromatography. As a result, the yield of the target TBSH was 71%.
実施例3〜14 実施例1に於て酸触媒,相間移動触媒,反応時間等の条
件を代えた他は、全く同様な操作を行った。結果を第1
表に示す。Examples 3 to 14 Except for changing the conditions such as the acid catalyst, the phase transfer catalyst and the reaction time in Example 1, the same operation was performed. First result
Shown in the table.
第1表においてTBC18.3g(0.1モル),23%水硫化ソーダ
水溶液31.7g(0.13モル),トルエン100g,反応温度50℃
の反応条件で行った。 In Table 1, TBC 18.3g (0.1mol), 23% sodium hydrosulfide aqueous solution 31.7g (0.13mol), toluene 100g, reaction temperature 50 ° C
The reaction conditions were as follows.
TBSHの収率(%)は、ガスクロマトグラフィーによる定
量分析で算出した。The yield (%) of TBSH was calculated by quantitative analysis by gas chromatography.
実施例15〜24 実施例1に於て、溶媒,相間移動触媒,酸触媒,温度,
時間等を代えた他は、全く同様な操作を行った。結果を
第2表に示す。Examples 15 to 24 In Example 1, the solvent, the phase transfer catalyst, the acid catalyst, the temperature,
Except for changing the time etc., the same operation was performed. The results are shown in Table 2.
第2表において、反応条件は、TBC18.3g(0.1モル),23
%水硫化ソーダ水溶液31.7g,溶媒各100gで行った。 In Table 2, the reaction conditions are TBC 18.3 g (0.1 mol), 23
% Sodium hydrosulfide aqueous solution 31.7 g, solvent 100 g each.
TBSHの収率(%)は、ガスクロマトグラフィーによる定
量分析で算出した。The yield (%) of TBSH was calculated by quantitative analysis by gas chromatography.
実施例25〜34 実施例1に於て、原料のベンジルハライド誘導体を代え
た他は、全く同様な操作を行った。結果を第3表に示
す。Examples 25 to 34 The same operation as in Example 1 was carried out except that the raw material benzyl halide derivative was replaced. The results are shown in Table 3.
第3表において、反応条件は原料(0.1モル),23%水硫
化ソーダ31.7g,トルエン100g反応温度50℃,反応時間1h
rで行った。 In Table 3, the reaction conditions are: raw material (0.1 mol), 23% sodium hydrosulfide 31.7g, toluene 100g reaction temperature 50 ° C, reaction time 1h
I went with r.
生成物の分析は、液体クロマトグラフィーの定量分析法
で行って、各生成物の収率(%)を算出した。The analysis of the products was performed by the quantitative analysis method of liquid chromatography, and the yield (%) of each product was calculated.
比較例1(米国特許2,456,588号記載の追試実施) 200ml四口反応フラスコにベンジルクロライド44.1g,含
水水硫化ソーダ(NaSH純度約70%)50g,水40gを仕込み
8時間還流させた。反応終了後、冷却しトルエン抽出し
た。トルエン溶液を水洗後、ガスクロマトグラフィーで
の定量を行った結果、目的とするベンジルメルカプタン
収率は31%であった。Comparative Example 1 (additional test described in US Pat. No. 2,456,588) A 200 ml four-neck reaction flask was charged with 44.1 g of benzyl chloride, 50 g of hydrous sodium hydrosulfide (NaSH purity about 70%), and 40 g of water and refluxed for 8 hours. After the reaction was completed, it was cooled and extracted with toluene. The toluene solution was washed with water and then quantified by gas chromatography. As a result, the target benzyl mercaptan yield was 31%.
比較例2〜5 実施例1に於て、酢酸の代りに米国特許2,456,588号記
載の添加物にかえた他は、全く同様に行った。結果を第
4表に示す。Comparative Examples 2 to 5 The procedure of Example 1 was repeated, except that the acetic acid was replaced by the additive described in US Pat. No. 2,456,588. The results are shown in Table 4.
第4表の結果より明らかなとおり、上記添加物を全く加
えない本発明の製造法(実施例2;収率71%)に比べて、
いずれも収率が低下している。 As is clear from the results in Table 4, as compared with the production method of the present invention (Example 2; yield 71%) in which the above additives are not added at all,
In each case, the yield is low.
フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C07C 323/16 323/22 // C07B 61/00 300 Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI technical display location C07C 323/16 323/22 // C07B 61/00 300
Claims (4)
て、 次式(II): で表されるベンジルハライド誘導体と、水硫化アルカリ
とを、水と非水溶性有機溶媒との混合溶媒中で、相間移
動触媒の存在下、反応させることを特徴とするベンジル
メルカプタン誘導体の製造法。 〔上記式中、Zはハロゲン原子を示し、Rは水素原子ま
たは低級アルキル基を示し、Xは炭素数1〜6の直鎖も
しくは分岐を有するアルキル基,炭素数1〜6の直鎖も
しくは分岐を有するアルコキシ基,炭素数3〜6のアル
ケニルオキシ基,低級ハロアルキル基,炭素数3〜6の
シクロアルキル基,ハロゲン原子, (但し、Yはハロゲン原子,低級アルキル基もしくは低
級ハロアルキル基を、mは0または1〜3の整数を示
し、mが2または3の場合は、Yは同一でも互いに異な
ってもよい。)またはトリメチルシリル基を示し、n
は、1〜3の整数を示す。nが2または3の場合はXは
同一でも互いに異なってもよい。〕。1. The following formula (I): In the method for producing a benzyl mercaptan derivative represented by the following formula (II): A method for producing a benzyl mercaptan derivative, which comprises reacting the benzyl halide derivative represented by and an alkali hydrosulfide in a mixed solvent of water and a water-insoluble organic solvent in the presence of a phase transfer catalyst. [In the above formula, Z represents a halogen atom, R represents a hydrogen atom or a lower alkyl group, X represents a linear or branched alkyl group having 1 to 6 carbon atoms, a linear or branched alkyl group having 1 to 6 carbon atoms. An alkoxy group having 3 to 6 carbon atoms, an alkenyloxy group having 3 to 6 carbon atoms, a lower haloalkyl group, a cycloalkyl group having 3 to 6 carbon atoms, a halogen atom, (However, Y represents a halogen atom, a lower alkyl group or a lower haloalkyl group, m represents an integer of 0 or 1 to 3, and when m is 2 or 3, Y may be the same or different from each other.) Trimethylsilyl group, n
Represents an integer of 1 to 3. When n is 2 or 3, X may be the same or different from each other. ].
て、 次式(II): で表されるベンジルハライド誘導体と、水硫化アルカリ
とを、水溶性有機溶媒中で、反応させることを特徴とす
るベンジルメルカプト誘導体の製造法。 〔上記式中、Zはハロゲン原子を示し、Rは水素原子ま
たは低級アルキル基を示し、Xは炭素数1〜6の直鎖も
しくは分岐を有するアルキル基,炭素数1〜6の直鎖も
しくは分岐を有するアルコキシ基,炭素数3〜6のアル
ケニルオキシ基,低級ハロアルキル基,炭素数3〜6の
シクロアルキル基,ハロゲン原子, (但し、Yはハロゲン原子,低級アルキル基もしくは低
級ハロアルキル基を、mは0または1〜3の整数を示
し、mが2または3の場合は、Yは同一でも互いに異な
ってもよい。)またはトリメチルシリル基を示し、n
は、1〜3の整数を示す。nが2または3の場合はXは
同一でも互いに異なってもよい。〕。2. The following formula (I): In the method for producing a benzyl mercaptan derivative represented by the following formula (II): A method for producing a benzylmercapto derivative, which comprises reacting the benzyl halide derivative represented by and an alkali hydrosulfide in a water-soluble organic solvent. [In the above formula, Z represents a halogen atom, R represents a hydrogen atom or a lower alkyl group, X represents a linear or branched alkyl group having 1 to 6 carbon atoms, a linear or branched alkyl group having 1 to 6 carbon atoms. An alkoxy group having 3 to 6 carbon atoms, an alkenyloxy group having 3 to 6 carbon atoms, a lower haloalkyl group, a cycloalkyl group having 3 to 6 carbon atoms, a halogen atom, (However, Y represents a halogen atom, a lower alkyl group or a lower haloalkyl group, m represents an integer of 0 or 1 to 3, and when m is 2 or 3, Y may be the same or different from each other.) Trimethylsilyl group, n
Represents an integer of 1 to 3. When n is 2 or 3, X may be the same or different from each other. ].
て、反応させる際に、酸触媒を添加することを特徴とす
る特許請求の範囲第1項または第2項記載の製造法。3. The production method according to claim 1 or 2, wherein an acid catalyst is added during the reaction in the claim 1 or 2.
リーブチルベンジルハライドである特許請求の範囲第3
項記載の製造法。4. The benzyl halide derivative is paratertiary butyl benzyl halide.
The manufacturing method described in the item.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61137852A JPH0710829B2 (en) | 1986-06-13 | 1986-06-13 | Method for producing benzyl mercaptan derivative |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP61137852A JPH0710829B2 (en) | 1986-06-13 | 1986-06-13 | Method for producing benzyl mercaptan derivative |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS62294652A JPS62294652A (en) | 1987-12-22 |
JPH0710829B2 true JPH0710829B2 (en) | 1995-02-08 |
Family
ID=15208295
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61137852A Expired - Fee Related JPH0710829B2 (en) | 1986-06-13 | 1986-06-13 | Method for producing benzyl mercaptan derivative |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0710829B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007204453A (en) * | 2006-02-06 | 2007-08-16 | Sumitomo Chemical Co Ltd | Method for producing alkenyl mercaptan |
JP2010120883A (en) * | 2008-11-20 | 2010-06-03 | Sumitomo Chemical Co Ltd | Method for producing alkenyl mercaptan |
JP2012056898A (en) * | 2010-09-09 | 2012-03-22 | Sumitomo Seika Chem Co Ltd | Method for producing alkane thiol |
-
1986
- 1986-06-13 JP JP61137852A patent/JPH0710829B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPS62294652A (en) | 1987-12-22 |
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