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JPS5948815B2 - Method for producing 1-chloro-1,3-diphenylpropane - Google Patents
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JPS5948815B2 - Method for producing 1-chloro-1,3-diphenylpropane - Google Patents

Method for producing 1-chloro-1,3-diphenylpropane

Info

Publication number
JPS5948815B2
JPS5948815B2 JP51049906A JP4990676A JPS5948815B2 JP S5948815 B2 JPS5948815 B2 JP S5948815B2 JP 51049906 A JP51049906 A JP 51049906A JP 4990676 A JP4990676 A JP 4990676A JP S5948815 B2 JPS5948815 B2 JP S5948815B2
Authority
JP
Japan
Prior art keywords
chloro
diphenylpropane
producing
styrene
reaction
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
JP51049906A
Other languages
Japanese (ja)
Other versions
JPS52133957A (en
Inventor
有亮 泉
昌人 岡田
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP51049906A priority Critical patent/JPS5948815B2/en
Publication of JPS52133957A publication Critical patent/JPS52133957A/en
Publication of JPS5948815B2 publication Critical patent/JPS5948815B2/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

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

Description

【発明の詳細な説明】 本発明は塩化ベンジルとスチレンとの反応に関し、その
1:1の付加物である1−クロルー1、3−ジフェニル
プロパンを収率よく製造することを目的とするものであ
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the reaction of benzyl chloride and styrene, and its purpose is to produce 1-chloro-1,3-diphenylpropane, which is a 1:1 adduct thereof, in a high yield. be.

従来、塩化物のオレフィン類との付加反応は古くからフ
リーデル・クラフト反応の一連の研究において良く研究
されている。
The addition reaction of chloride with olefins has been well studied in the Friedel-Crafts reaction series for a long time.

例えばα−クロルエチルベンゼンはイソブチレンとZn
Cl2触媒により95%の収率で1:1の付加物である
2−メチルー2−クロルー4−フェニルペンタンを与え
る。又スチレンとの反応では50%の収率で1−クロル
ー1、3−ジフェニルブタンを与える(G、A。DLa
h3゛FriedelCraftsandRelate
dRoactions″、vol、2、Poフ 768
3IntersciencePublishers、I
nc、、NewYork、)。しかしながら、塩化ベン
ジルの如き1級の塩化物はオレフィン類に対して付加反
応を起さず、該オレフィン類が塩化ベンジルの芳香環へ
アルキル化される。5 しかるに、本発明者らはホスフ
オニウム塩と金属鉄とから成る触媒を用いることにより
、上記フリーデル・クラフト触媒では進行しない塩化ベ
ンジルとスチレンとの付刀口反応が可能であることを見
出し、本発明を提案するに至つたものである。
For example, α-chloroethylbenzene is a mixture of isobutylene and Zn.
Cl2 catalysis gives the 1:1 adduct 2-methyl-2-chloro-4-phenylpentane in 95% yield. In addition, reaction with styrene gives 1-chloro-1,3-diphenylbutane with a yield of 50% (G, A. DLa
h3゛Friedel CraftsandRelate
dRoactions'', vol, 2, Pofu 768
3IntersciencePublishers, I
nc, New York). However, primary chlorides such as benzyl chloride do not undergo addition reactions with olefins, and the olefins are alkylated to the aromatic ring of benzyl chloride. 5 However, the present inventors have discovered that by using a catalyst consisting of a phosphonium salt and metallic iron, it is possible to carry out the side-by-side reaction between benzyl chloride and styrene that does not proceed with the Friedel-Crafts catalyst, and has developed the present invention. This led us to propose the following.

0 本発明における触媒成分のうち、ホスフオニウ+−
ム塩としては一般的には〔R7R2R8P−R4〕 C
l(R、、R2、R3、R4はいずれもアルキル基又は
アリール基)で表わされるも・ので特に制限されないが
、その経済性及び取り扱い易さからトリフエニ5ルホス
フインから誘導されるホスフオニウム塩+〔ph3P−
R′)Cl(phはフェニル基、Rはアルキル基又はア
リール基)が好適である。
0 Of the catalyst components in the present invention, phosphoniu+-
In general, [R7R2R8P-R4] C
(R, , R2, R3, R4 are all alkyl groups or aryl groups. −
R')Cl (ph is a phenyl group, R is an alkyl group or an aryl group) is preferred.

また、他の触媒成分である金属鉄としては粒状で粒子径
の小さいほど好ましく、一般には20メッシュ以下0特
に200メッシュ以下の鉄粉が好適に用いられる。上記
触媒成分の混合割合は、一般に金属鉄1ミリグラム原子
に対してホスフオニウム塩0.1〜100ミリモルの範
囲で使用されるが、該触媒成分を反応後にホスフオニウ
ム塩とハロゲン化第二・5鉄の錯塩として回収する場合
には両触媒成分を等モルの割合で使用することが望まし
い。本発明の反応系において、上記触媒の濃度はスチレ
ン1モルに対してホスフオニウム塩0.001〜0.0
5モルの割合で充分であり、これ以上の高濃度でもよい
が経済的でなく,一般にはスチレン1モルに対してホス
フオニウム塩0.005〜3モルの割合が実用的な濃度
で好ましい。
Further, the metal iron, which is another catalyst component, is preferably granular and has a smaller particle diameter, and generally iron powder of 20 mesh or less, particularly 200 mesh or less, is preferably used. The mixing ratio of the above catalyst components is generally in the range of 0.1 to 100 mmol of phosphonium salt per 1 milligram atom of metallic iron. When recovering as a complex salt, it is desirable to use both catalyst components in an equimolar ratio. In the reaction system of the present invention, the concentration of the catalyst is 0.001 to 0.0 phosphonium salt per mole of styrene.
A ratio of 5 moles is sufficient, and a higher concentration may be used, but it is not economical, and generally a practical concentration of 0.005 to 3 moles of phosphonium salt per mole of styrene is preferred.

また,本発明において反応に供する塩化ベンジルとスチ
レンとの割合は約1:1〜約10;1,好ましくは約2
:1〜約4:1の範囲から任意に選択することができる
Further, in the present invention, the ratio of benzyl chloride and styrene to be subjected to the reaction is about 1:1 to about 10:1, preferably about 2:1.
:1 to about 4:1.

そのほか,本発明の反応における条件は特に制限されず
、通常の装置,手段の下に実施すればよく,一般に常圧
〜加圧下,約95〜130℃好ましくは105〜115
℃の範囲で実施される。なお、本発明の反応に際しホス
フオニウム塩を溶解し易い溶媒,例えばメタノール,エ
タノール,イソプロパノール等のアルコール類,アセト
ニトリル,ジメチルホルムアミド等の非プロトン極性溶
媒,そのほか酢酸メチル,酢酸エチル等を添加すること
によつて,塩化ベンジルとスチレンの1:1付加生成物
である1−クロル−1,3−ジフエニルプロパンの収率
を向上させることができる。
In addition, the conditions for the reaction of the present invention are not particularly limited, and may be carried out using conventional equipment and means, generally under normal pressure to pressurization, about 95 to 130°C, preferably 105 to 115°C.
It is carried out in the range of °C. In addition, during the reaction of the present invention, solvents that easily dissolve the phosphonium salt, such as alcohols such as methanol, ethanol, and isopropanol, aprotic polar solvents such as acetonitrile and dimethylformamide, and other solvents such as methyl acetate and ethyl acetate may be added. Therefore, the yield of 1-chloro-1,3-diphenylpropane, which is a 1:1 addition product of benzyl chloride and styrene, can be improved.

本願で得られる1−クロル−1,3−ジフエニルプロパ
ンは種々の原料又は中間原料として使用され、例えば向
神経剤,精神療法剤等に使用される1−(1,3−ジア
リールプロピン)ピペラジンの原料として好適に使用さ
れる。実施例 1 塩化ベンジル40d(0.348モノリ,スチレン11
.4d(0.1モル)及び触媒としてトリフエニルベン
ジルホスフオニウムクロライド〔Ph3P一CH,ph
)+Cf777Tflf(2ミリモノリと金属鉄112
W9(2ミリグラム原子)とを丸底フラスコに仕込んだ
1-Chlor-1,3-diphenylpropane obtained in the present application is used as various raw materials or intermediate raw materials, such as 1-(1,3-diarylpropyne) used in neurotropic agents, psychotherapeutic agents, etc. It is suitably used as a raw material for piperazine. Example 1 Benzyl chloride 40d (0.348 mono, styrene 11
.. 4d (0.1 mol) and triphenylbenzylphosphonium chloride [Ph3P1CH, ph
) + Cf777Tflf (2mm monolith and metal iron 112
W9 (2 milligram atoms) was charged into a round bottom flask.

反応系内を窒素ガスで置換した後.マグネチツクスター
ラ一で攪拌しながら、110℃の温度で4時間反応を行
つた。冷却後に触媒残渣等を除去するために水洗を2回
行つた。
After replacing the reaction system with nitrogen gas. The reaction was carried out at a temperature of 110° C. for 4 hours while stirring with a magnetic stirrer. After cooling, water washing was performed twice to remove catalyst residues and the like.

次いで,反応液を減圧蒸留することによつて沸点134
〜135℃/21m1H9の留分9.5gを留出した。
これはガスクロマトグラフイ,赤外線(IR),核磁気
共鳴(NMR)スペクトルより1−クロル−1,3−ジ
フエニルプロパンであることを確認した。スチレンから
の収率は41.2モル?である。実施例 2 実施例1におけるトリフエニルベシジルホスフオニウム
クロライドの代りにトリフエニルクロルメチルホスフオ
ニウムクロライド〔Ph,P一CH,Cl′)+Cf7
63mg(2ミリモノリを用いた以外は、実施例1と全
く同様に反応を実施した。
Next, the reaction solution was distilled under reduced pressure to a boiling point of 134
A fraction of 9.5 g was distilled out at ~135°C/21mlH9.
This was confirmed to be 1-chloro-1,3-diphenylpropane by gas chromatography, infrared ray (IR), and nuclear magnetic resonance (NMR) spectra. The yield from styrene is 41.2 moles? It is. Example 2 Instead of triphenyl besidyl phosphonium chloride in Example 1, triphenyl chloromethyl phosphonium chloride [Ph, P CH, Cl') + Cf7
The reaction was carried out in exactly the same manner as in Example 1, except that 63 mg (2 mm) was used.

Claims (1)

【特許請求の範囲】 1 塩化ベンジルとスチレンとをホスフオニウム塩と金
属鉄とよりなる触媒の存在下に反応させることを特徴と
する1−クロル−1,3−ジフェニルプロパンの製造方
法。 2 ホスフオニウム塩がトリフェニルホスフィンから誘
導されるホスフオニウム塩〔ph_3P−R〕^+Cl
^−(phはフェニル基、Rはアルキル基またはアリー
ル基)である特許請求の範囲第1項記載の1−クロル−
1,3−ジフェニルプロパンの製造方法。 3 金属鉄が粒子径20メッシュ以下の鉄粉である特許
請求の範囲第1項記載の1−クロル−1,3−ジフェニ
ルプロパンの製造方法。 4 反応温度が95〜135℃である特許請求の範囲第
1項記載の1−クロル−1,3−ジフェニルプロパンの
製造方法。
[Scope of Claims] 1. A method for producing 1-chloro-1,3-diphenylpropane, which comprises reacting benzyl chloride and styrene in the presence of a catalyst consisting of a phosphonium salt and metal iron. 2 Phosphonium salt derived from triphenylphosphine [ph_3P-R]^+Cl
1-chloro- according to claim 1, which is ^- (ph is a phenyl group, R is an alkyl group or an aryl group)
A method for producing 1,3-diphenylpropane. 3. The method for producing 1-chloro-1,3-diphenylpropane according to claim 1, wherein the metallic iron is iron powder with a particle size of 20 mesh or less. 4. The method for producing 1-chloro-1,3-diphenylpropane according to claim 1, wherein the reaction temperature is 95 to 135°C.
JP51049906A 1976-05-04 1976-05-04 Method for producing 1-chloro-1,3-diphenylpropane Expired JPS5948815B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51049906A JPS5948815B2 (en) 1976-05-04 1976-05-04 Method for producing 1-chloro-1,3-diphenylpropane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51049906A JPS5948815B2 (en) 1976-05-04 1976-05-04 Method for producing 1-chloro-1,3-diphenylpropane

Publications (2)

Publication Number Publication Date
JPS52133957A JPS52133957A (en) 1977-11-09
JPS5948815B2 true JPS5948815B2 (en) 1984-11-29

Family

ID=12844043

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51049906A Expired JPS5948815B2 (en) 1976-05-04 1976-05-04 Method for producing 1-chloro-1,3-diphenylpropane

Country Status (1)

Country Link
JP (1) JPS5948815B2 (en)

Also Published As

Publication number Publication date
JPS52133957A (en) 1977-11-09

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