JPH07246338A - Lewis acid catalyst - Google Patents

Lewis acid catalyst

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Publication number
JPH07246338A
JPH07246338A JP6040839A JP4083994A JPH07246338A JP H07246338 A JPH07246338 A JP H07246338A JP 6040839 A JP6040839 A JP 6040839A JP 4083994 A JP4083994 A JP 4083994A JP H07246338 A JPH07246338 A JP H07246338A
Authority
JP
Japan
Prior art keywords
lewis acid
acid catalyst
reaction
metal
general formula
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.)
Granted
Application number
JP6040839A
Other languages
Japanese (ja)
Other versions
JP3166959B2 (en
Inventor
Hiroshi Kobayashi
宏 小林
Susumu Shiyou
進 聶
Takaaki Sonoda
高明 園田
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.)
Central Glass Co Ltd
Original Assignee
Central Glass 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 Central Glass Co Ltd filed Critical Central Glass Co Ltd
Priority to JP04083994A priority Critical patent/JP3166959B2/en
Publication of JPH07246338A publication Critical patent/JPH07246338A/en
Application granted granted Critical
Publication of JP3166959B2 publication Critical patent/JP3166959B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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    • 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

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  • Catalysts (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

PURPOSE:To obtain a Lewis acid catalyst used for org. synthesis reactions of medicines agrochemicals, a liq. crystal, a polymer or their intermediates. CONSTITUTION:This Lewis acid catalyst is made of a compd. represented by the general formula M [RfSO2-N-SO2Rf']n, or M[RfS02-N-S02Rf']n.mH2O [where each of Rf and Rf' is a 1-8C perfluoroalkyl, M is an element selected from among alkali metals, alkaline earth metals, transition metals, rare earth elements, Al, Ga, Ir, Tl, Si, Ge, Sn, Pb, As, Sb, Bi, Se and Te, (n) is an integer equal to the valance of M and (m) is a natural number of 0.5-20].

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は医薬、農薬、液晶、ポリ
マーあるいはそれらの中間体等の有機化合物の合成反応
に有用に利用されるルイス酸触媒に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a Lewis acid catalyst which is useful in the synthetic reaction of organic compounds such as pharmaceuticals, agricultural chemicals, liquid crystals, polymers and their intermediates.

【0002】[0002]

【従来の技術および解決すべき問題点】従来、金属塩を
ルイス酸触媒として有機反応に用いる場合は、通常のハ
ロゲン化物、酢酸塩、炭酸塩などの金属塩ではジクロロ
メタンなどの非極性溶媒に対する溶解度が極めて小さい
ために、金属イオンに対する配位能が大きいエーテルや
アセトニトリルなどの非プロトン性極性溶媒を用いる必
要がある。しかしながらこれらの極性溶媒中では金属イ
オンに溶媒分子が強く配位するために反応基質に対する
金属イオンの親電子的なルイス酸触媒活性が極端に減少
してしまう。
2. Description of the Related Art Conventionally, when a metal salt is used as an Lewis acid catalyst in an organic reaction, the solubility of ordinary metal salts such as halides, acetates and carbonates in a non-polar solvent such as dichloromethane is high. Since it is extremely small, it is necessary to use an aprotic polar solvent such as ether or acetonitrile which has a large coordination ability for metal ions. However, in these polar solvents, the solvent molecule strongly coordinates with the metal ion, so that the electrophilic Lewis acid catalytic activity of the metal ion with respect to the reaction substrate is extremely reduced.

【0003】本発明の目的とするところは、上記問題点
に鑑み、求電子反応による有機反応における触媒活性を
増大させるルイス酸触媒を提供することにある。
In view of the above problems, it is an object of the present invention to provide a Lewis acid catalyst which increases the catalytic activity in an organic reaction by an electrophilic reaction.

【0004】[0004]

【問題点を解決するための手段】本発明者らは、鋭意検
討の結果、種々のM[RfSO2 −N−SO2 Rf’]
n (ペルフルオロアルカンスルホニルイミド金属塩)な
る金属塩及びその水和物を用いることにより、種々の求
電子反応の有機反応において反応速度が促進され、特に
異性体を生成する反応においては、その選択性を向上さ
せることを見出し本発明に到達した。
[Means for Solving the Problems]
As a result of discussion, various M [RfSO2-N-SO2Rf ']
n(Perfluoroalkanesulfonylimide metal salt)
By using metal salts and hydrates of
The reaction rate is accelerated in the organic reaction of the electron reaction,
In a reaction that produces an isomer, its selectivity is improved.
The inventors have reached the present invention by finding that they can.

【0005】本発明のペルフルオロアルカンスルホニル
イミド金属塩は、フランス特許2527602号、26
06217号にイオン伝導材料としての利用のみが開示
されており、その他触媒として利用されたという文献、
あるいは特許の記述はなく、ルイス酸触媒としての効果
を見出したことは意義あることである。
The perfluoroalkanesulfonylimide metal salts of the present invention are described in French Patent No. 2527602, 26.
No. 06217 discloses use only as an ion conductive material, and is used as a catalyst for other catalysts,
Alternatively, there is no description in the patent, and it is significant that the effect as a Lewis acid catalyst was found.

【0006】本発明の触媒として用いられる一般式
(I)、一般式(II)で示されるペルフルオロアルカ
ンスルホニルイミド金属塩及びその水和物は、ペルフル
オロアルカンスルホニルイミド酸H[RfSO2 −N−
SO2 Rf’]と該当する金属の炭酸塩、酸化物、水酸
化物あるいはそれらの混合物から選ばれる化合物を用い
て水溶液中で温度20〜100℃で反応させ余剰の水を
加熱あるいは減圧下で乾燥し合成させる。
The perfluoroalkanesulfonylimide metal salts represented by the general formulas (I) and (II) and their hydrates used as the catalyst of the present invention are perfluoroalkanesulfonylimidic acid H [RfSO 2 —N-
SO 2 Rf ′] and a compound selected from carbonates, oxides, hydroxides or a mixture thereof of the corresponding metal are reacted in an aqueous solution at a temperature of 20 to 100 ° C. and excess water is heated or under reduced pressure. Dry and synthesize.

【0007】これら合成された金属塩およびその水和物
は求電子反応の有機合成反応で有れば利用が可能で、た
とえばディールス−アルダー反応、マイケル付加反応、
フリーデル−クラフト反応等である。これらの反応に使
用すると反応速度が加速され、また収率が向上する。さ
らに異性体を生成する反応においては選択性を向上させ
ることができる。この理由としてはペルフルオロアルカ
ンスルホニルイミドイオン[RfSO2 −N−SO2
f’]- を対アニオンとする金属塩の場合は、ジクロロ
メタンなどの非極性溶媒中での溶解度が比較的大きいと
いう含フッ素有機化合物の一般的な特徴に加えて、フッ
素原子の強力な電子吸引力によって含フッ素イミドイオ
ンが安定化され金属イオンとの間のイオン結合が通常の
金属塩に比べてはるかに小さいという特徴を持ってい
る。この結果非極性溶媒中では脱溶媒和した金属イオン
の親電子性が大きくなり、これらの金属塩のルイス酸触
媒活性が非常に増大することによる。
These synthesized metal salts and hydrates thereof can be used as long as they are organic synthesis reactions of electrophilic reaction. For example, Diels-Alder reaction, Michael addition reaction,
Friedel-Crafts reaction and the like. When used in these reactions, the reaction rate is accelerated and the yield is improved. Further, the selectivity can be improved in the reaction for producing the isomer. The reason for this is that perfluoroalkanesulfonylimide ion [RfSO 2 —N—SO 2 R
In the case of a metal salt having f ′] as a counter anion, in addition to the general characteristic of a fluorine-containing organic compound that solubility in a non-polar solvent such as dichloromethane is relatively large, strong electron withdrawing of a fluorine atom is performed. It is characterized in that the fluorinated imide ion is stabilized by the force, and the ionic bond with the metal ion is much smaller than that of ordinary metal salts. As a result, the electrophilicity of the desolvated metal ion is increased in the nonpolar solvent, and the Lewis acid catalytic activity of these metal salts is greatly increased.

【0008】触媒としての添加量は反応基質に対して
0.1〜20mol%で触媒能が現れるが、実用的な反
応速度を得ること、また経済性を考慮した場合、添加量
は1〜10mol%が好ましい。また溶媒は炭化水素、
ハロゲン化炭化水素、エーテル等の使用が可能である。
The catalytic activity appears when the amount added as a catalyst is 0.1 to 20 mol% with respect to the reaction substrate, but the amount added is 1 to 10 mol in consideration of obtaining a practical reaction rate and economical efficiency. % Is preferred. The solvent is hydrocarbon,
It is possible to use halogenated hydrocarbons, ethers and the like.

【0009】[0009]

【実施例】以下、実施例において具体的に説明するが係
る実施例に限定されるものではない。
EXAMPLES Hereinafter, the examples will be specifically described, but the examples are not limited thereto.

【0010】実施例1 MgCO3 ・Mg(OH)2 ・5H2 O:0.2397
gをフラスコにいれ、ビストリフルオロメタンスルホニ
ルイミド酸(HN(CF3 SO2 2 ):1.5gを水
5gで溶かして攪拌しながら滴下した。20℃で2時間
反応させた後沈澱物を濾別し水溶液を50℃、0.4m
mHgで乾燥しMg((CF3 SO2 2 N)2 ・3H
2 Oを得た。また、さらに50℃、10-5mmHgで1
5時間乾燥させMg((CF3 SO2 2 N)2 1.5
gを得た。
Example 1 MgCO3・ Mg (OH)2・ 5H2O: 0.2397
Add g to the flask and add bistrifluoromethanesulfone.
Lumidic acid (HN (CF3SO2)2): 1.5 g water
It was dissolved in 5 g and added dropwise with stirring. 2 hours at 20 ° C
After the reaction, the precipitate was separated by filtration and the aqueous solution was heated at 50 ° C. for 0.4 m.
After drying with mHg, Mg ((CF3SO2) 2N)2・ 3H
2O was obtained. In addition, further 50 ℃, 10-Five1 in mmHg
After drying for 5 hours, Mg ((CF3SO2)2N)21.5
g was obtained.

【0011】実施例2 CaCO3 :0.2289gをフラスコにいれ、ビスト
リフルオロメタンスルホニルイミド酸(HN(CF3
2 2 ):1.2907gを水5gで溶かして攪拌し
ながら滴下した。20℃で反応させた後沈澱物を濾別し
水溶液を20℃、10-5mmHgで乾燥させCa((C
3 SO2 2 N)2 ・1.5H2 Oを得た。さらに1
35℃、10-5mmHgで15時間乾燥させCa((C
3 SO 2 2 N)2 1.3378gを得た。
Example 2 CaCO3: 0.2289g in a flask
Lifluoromethanesulfonylimidic acid (HN (CF3S
O2)2): 1.2907 g was dissolved in 5 g of water and stirred
While dripping. After reacting at 20 ° C., the precipitate was filtered off
Aqueous solution at 20 ℃, 10-FiveDry with mmHg Ca ((C
F3SO2)2N)2・ 1.5H2O was obtained. 1 more
35 ° C, 10-FiveAfter drying for 15 hours at mmHg, Ca ((C
F3SO 2)2N)21.3378 g was obtained.

【0012】実施例3 BaCO3 :0.4849gをフラスコにいれ、ビスト
リフルオロメタンスルホニルイミド酸(HN(CF3
2 2 ):1.3865gを水5gで溶かして攪拌し
ながら滴下した。40℃で反応させた後沈澱物を濾別し
水溶液を60℃、10-3mmHgで乾燥させBa((C
3 SO2 2 N)2 ・1.5H2 Oを得た。さらに1
50℃、10-5mmHgで15時間乾燥させBa((C
3 SO 2 2 N)2 1.6338gを得た。
Example 3 BaCO3: Add 0.4849g to the flask and bistro
Lifluoromethanesulfonylimidic acid (HN (CF3S
O2)2): 1.3865 g was dissolved in 5 g of water and stirred
While dripping. After reacting at 40 ° C., the precipitate was filtered off
Aqueous solution at 60 ℃, 10-3After drying with mmHg, Ba ((C
F3SO2)2N)2・ 1.5H2O was obtained. 1 more
50 ° C, 10-FiveAfter drying at mmHg for 15 hours, Ba ((C
F3SO 2)2N)21.6338 g was obtained.

【0013】実施例4 ZnO:0.2033gをフラスコにいれ、ビストリフ
ルオロメタンスルホニルイミド酸(HN(CF3
2 2 ):1.420gを水5gで溶かして攪拌しな
がら滴下した。20℃で反応させた後沈澱物を濾別し水
溶液を40℃、0.4mmHgで乾燥させZn((CF
3 SO2 2 N)2 ・7H2 Oを得た。さらに100
℃、10-6mmHgで15時間乾燥させZn((CF3
SO2 2 N) 2 1.7966gを得た。
Example 4 ZnO: 0.2033 g was placed in a flask and bistrif.
Luoromethanesulfonylimidic acid (HN (CF3S
O2)2): Dissolve 1.420 g with 5 g of water and do not stir
It was dripped. After reacting at 20 ° C, the precipitate was filtered off and filtered with water.
The solution was dried at 40 ° C. and 0.4 mmHg, and Zn ((CF
3SO2)2N)2・ 7H2O was obtained. 100 more
℃, 10-6After drying for 15 hours at mmHg, Zn ((CF3
SO2)2N) 2Obtained was 1.7966 g.

【0014】実施例5 La2 3 :0.4208gをフラスコにいれ、ビスト
リフルオロメタンスルホニルイミド酸(HN(CF3
2 2 ):2.1832gを水5gで溶かして攪拌し
ながら滴下した。100℃1時間反応させた後沈澱物を
濾別し水溶液を70℃、0.4mmHgで乾燥させLa
((CF3 SO2 2 N)3 ・3H2 Oを得た。さらに
60℃、10-3mmHgで15時間乾燥させLa((C
3 SO 2 2 N)3 2.5444gを得た。
Example 5 La2O3: Add 0.4208g to the flask, bisto
Lifluoromethanesulfonylimidic acid (HN (CF3S
O2)2): 2.1832 g was dissolved in 5 g of water and stirred
While dripping. After reacting at 100 ° C for 1 hour, the precipitate was removed.
It is filtered off and the aqueous solution is dried at 70 ° C. and 0.4 mmHg to obtain La.
((CF3SO2)2N)3・ 3H2O was obtained. further
60 ° C, 10-3Lam ((C
F3SO 2)2N)32.5444 g was obtained.

【0015】実施例6、比較例1 メチルビニルケトン392.0mgに内部標準としてデ
カン392.2mgとCH2 Cl2 25mlを加え、さ
らにシクロペンタジエン594.0mgとCH 2 Cl2
25mlを加えた。この混合溶液を17.7ml採取し
実施例1で示したMg((CF3 SO2 2 N)2
0.0173mol(1mol%)加えた。生成物であ
る5−アセチルビシクロ〔2,2,1〕ヘプタ−2−エ
ンの増加量をガスクロマトグラフィーによって分析し、
反応速度定数および転化率を求めた。反応は、選択的に
進行した。また生成物のエンド体およびエキソ体の比に
ついては反応終了後の生成物のガスクロマトグラフィー
によって決定した。以下の表1にこの反応による反応速
度定数、転化率および生成物のエンド体およびエキソ体
の比を示す。また比較のために触媒無添加時の場合の反
応速度定数、転化率および生成物のエンド体およびエキ
ソ体の比を示す。反応温度はいずれも20℃に保った。
Example 6, Comparative Example 1 392.0 mg of methyl vinyl ketone was used as an internal standard.
392.9 mg of can and CH2Cl2Add 25 ml,
Cyclopentadiene 594.0 mg and CH 2Cl2
25 ml was added. 17.7 ml of this mixed solution was sampled
The Mg ((CF3SO2)2N)2To
0.0173 mol (1 mol%) was added. Is a product
5-acetylbicyclo [2,2,1] hept-2-e
Gas chromatographic analysis for increased amounts of
The reaction rate constant and conversion rate were determined. The reaction is selective
Progressed. In addition, the ratio of the endo-form and exo-form of the product
Gas chromatography of the product after the reaction
Determined by The reaction speed of this reaction is shown in Table 1 below.
Degree constant, conversion and endo- and exo-forms of the product
The ratio of In addition, for comparison, the reaction when no catalyst was added
Response rate, conversion and end product and exhaust of product
The ratio of the so body is shown. The reaction temperature was kept at 20 ° C. in all cases.

【0016】[0016]

【表1】 [Table 1]

【0017】実施例7〜16、比較例2 実施例6と同様の反応で実施例1〜5で合成した化合物
の触媒効果を溶媒別(ジクロロメタン、ジエチルエーテ
ル)に表2、表3に示した。それぞれに触媒濃度、反応
速度定数、転化率および生成物のエンド体およびエキソ
体の比を示す。
Examples 7 to 16 and Comparative Example 2 Tables 2 and 3 show the catalytic effects of the compounds synthesized in Examples 1 to 5 in the same reaction as in Example 6 for each solvent (dichloromethane, diethyl ether). . The catalyst concentration, the reaction rate constant, the conversion rate, and the ratio of the endo-form and the exo-form of the product are shown for each.

【0018】[0018]

【表2】 [Table 2]

【0019】[0019]

【表3】 [Table 3]

【0020】[0020]

【発明の効果】本発明におけるルイス酸触媒を用いるこ
とにより、求電子反応による有機合成反応において、目
的物の生成速度が促進され、收率の向上をもたらす。ま
た、異性体の生成においては、その選択性を大幅に向上
させることができる。
EFFECT OF THE INVENTION By using the Lewis acid catalyst of the present invention, the production rate of the target substance is promoted in the organic synthesis reaction by the electrophilic reaction, and the yield is improved. In addition, in the production of isomers, the selectivity can be greatly improved.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 一般式(I) M[RfSO2 −N−SO2 Rf’]n ・・・(I) (Rf及びRf’は、炭素原子数1〜8のペルフルオロ
アルキル基を表し、Mはアルカリ金属、アルカリ土類金
属、遷移金属、希土類、アルミニウム、ガリウム、イリ
ジウム、タリウム、ケイ素、ゲルマニウム、スズ、鉛、
ヒ素、アンチモン、ビスマス、セレン、テルルから選ば
れた元素を表し、nは該当する金属の原子価と同数の整
数を表す)で示されるルイス酸触媒。
1. General formula (I) M [RfSO 2 —N—SO 2 Rf ′] n ... (I) (Rf and Rf ′ represent a perfluoroalkyl group having 1 to 8 carbon atoms, and M Is an alkali metal, alkaline earth metal, transition metal, rare earth, aluminum, gallium, iridium, thallium, silicon, germanium, tin, lead,
Lewis acid catalyst represented by an element selected from arsenic, antimony, bismuth, selenium, and tellurium, and n represents an integer equal to the valence of the corresponding metal.
【請求項2】 一般式(II) M[RfSO2 −N−SO2 Rf’]n ・mH2 O ・・・(II) (Rf及びRf’は、炭素原子数1〜8のペルフルオロ
アルキル基を表し、Mはアルカリ金属、アルカリ土類金
属、遷移金属、希土類、アルミニウム、ガリウム、イリ
ジウム、タリウム、ケイ素、ゲルマニウム、スズ、鉛、
ヒ素、アンチモン、ビスマス、セレン、テルルから選ば
れた元素を表し、nは該当する金属の原子価と同数の整
数を表し、mは0.5〜20の自然数を表す)で示され
るルイス酸触媒。
2. General formula (II) M [RfSO 2 —N—SO 2 Rf ′] n · mH 2 O (II) (Rf and Rf ′ are perfluoroalkyl groups having 1 to 8 carbon atoms. Represents M, alkali metal, alkaline earth metal, transition metal, rare earth, aluminum, gallium, iridium, thallium, silicon, germanium, tin, lead,
Lewis acid catalyst represented by an element selected from arsenic, antimony, bismuth, selenium, and tellurium, n is an integer having the same number as the valence of the corresponding metal, and m is a natural number of 0.5 to 20). .
【請求項3】 Rf及びRf’の炭素原子数が1である
請求項1または請求項2に記載のルイス酸触媒。
3. The Lewis acid catalyst according to claim 1, wherein Rf and Rf ′ have 1 carbon atom.
JP04083994A 1994-03-11 1994-03-11 Lewis acid catalyst Expired - Fee Related JP3166959B2 (en)

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Publication Number Publication Date
JPH07246338A true JPH07246338A (en) 1995-09-26
JP3166959B2 JP3166959B2 (en) 2001-05-14

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Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998021197A3 (en) * 1996-11-11 1998-07-23 Hoffmann La Roche PROCESS FOR MANUFACTURING d,l-α-TOCOPHEROL
US6235921B1 (en) 1995-02-13 2001-05-22 Central Glass Company, Limited Amines or salts thereof and methods of preparing same
EP1344772A1 (en) * 2000-12-15 2003-09-17 Japan Science and Technology Corporation Arylbis (perfluoroalkylsulfonyl) methane, metal salt of the same, and processes for producing these
JP2004200015A (en) * 2002-12-19 2004-07-15 Sanyo Electric Co Ltd Electrolyte for nonaqueous battery, its manufacturing method, and nonaqueous battery electrolytic solution
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