CN1084725C - α-氯烷芳酮的制备方法 - Google Patents

α-氯烷芳酮的制备方法 Download PDF

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CN1084725C
CN1084725C CN96108016A CN96108016A CN1084725C CN 1084725 C CN1084725 C CN 1084725C CN 96108016 A CN96108016 A CN 96108016A CN 96108016 A CN96108016 A CN 96108016A CN 1084725 C CN1084725 C CN 1084725C
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alkyl
aryl ketones
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alcohol
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CN1142483A (zh
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W·西格尔
W·多布勒
M·约翰
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C45/00Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
    • C07C45/61Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups
    • C07C45/63Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reactions not involving the formation of >C = O groups by introduction of halogen; by substitution of halogen atoms by other halogen atoms
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    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C201/00Preparation of esters of nitric or nitrous acid or of compounds containing nitro or nitroso groups bound to a carbon skeleton
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Abstract

本发明介绍了一种用硫酰氯使通式II的烷芳酮类在脂肪醇存在下进行氯化,制备通式I的α-氯烷芳酮类的方法其中,n为1至5,相互独立的R1为H、烷基、烷氧基、芳基、芳氧基、酰氧式、酰氨基、卤素或硝基、相互独立的R2、R3为H、烷基或芳基。

Description

α-氯烷芳酮的制备方法
本发明涉及一种制备α-氯烷芳酮类的新方法。
α-氯烷芳酮类是作为合成药物和农作物保护有效化合物的中间体。它们要预先特别是通过烷芳酮类和氯化剂进行反应来制取。
Lands等人(J.Med.Chem.35(1992)3081-3084)揭露了下述反应,其生成的产物B的产率是41%。
Figure C9610801600031
我们自己用SO2Cl2为氯化剂做的实验表明,在氯化过程中,随反应过程而定,不是产率令人不满意,就是选择性过低。
本发明的目的就是给出一种通过用SO2Cl2氯化烷芳酮类制备α-氯烷芳酮类的有效方法,其中又不会出现上述缺点。
我们已经发现通过用硫酰氯对通式II
Figure C9610801600041
的烷芳酮类在脂族醇存在下的卤化作用制备通式I的α-氯烷芳酮类,就能达到此目的。
Figure C9610801600042
其中n为1-5,相互独立的R1为H、烷基、烷氧基、芳基、芳氧基、酰氧基、酰氨基卤素或硝基,相互独立的R2,3为H、烷基或芳基。饱和或不饱和脂族醇适合于本发明的方法。最好使用饱和的无支链或支链醇类,尤其是那些有1-10个碳原子的。
最好的醇类是甲醇、乙醇、丙醇、异丙醇、丁醇或异丁醇。
按照本发明方法里使用的醇类,既可以单独一种使用,也可以混合使用。
如果每摩尔烷芳酮使用0.1-10摩尔量的脂族醇,最好是2-6摩尔,那么就能得到好的结果。比那些指定值低的摩尔比通常会引起明显的副反应,而摩尔比高通常导致转化不完全。
通常每摩尔烷基酮II使用的硫酰氯量为1-2摩尔,最好是1.0--1.5摩尔。
硫酰氯也可以使用这些特定量之外的量,但不能引起按照本发明方法的改进。
因为式I的α-氯烷芳酮类通常是固体,所以最好在溶剂里进行反应。合适的溶剂是所有那些易溶解所用烷基酮类II和生成的α-氯烷芳酮类I二者、又不在反应条件下参加任何与硫酰氯发生的反应的溶剂。芳烃类,例如苯、甲苯、乙苯、二甲苯,例如邻二甲苯和1,2,3,4-四氢化萘,卤代芳族类,例如氯苯和二氯苯,例如1,2-二氯苯,分子式CnH2n+2的/饱和脂族烃类,其中n=5-20,例如己烷、庚烷和辛烷,以及氯代脂族烃,例如二氯甲烷、氯仿、四氯甲烷、1,1-二氯乙烷、1,2-二氯乙烷、1,1,1-三氯乙烷和1,1,2-三氯乙烷及它们的混合物都特别合适。
因为反应压力增加或减少都不会对选择性、产率和工艺技术有任何益处,所以反应最好在常压下进行。
反应在-80℃至+100℃的温度内,最好在0℃至50℃的范围内进行。此范围之外的反应温度对选择性、产率和工艺技术不会出现明显的好处,但却会由于冷却或加热所需能量的增加而引起不必要的费用增加。
反应可以在适当的设备中以分批或连续形式进行。
用于本发明方法中的式II烷芳酮类是已知的商品,或已知—例如按照Friedel-Crafts法(Houben Weyl"Methoden derorganischenChemie"(有机化学方法)Georg Thieme Verlag,Stuttgart 1973,7/2a卷第一部分,第23页-107页和135-154页)一从芳烃和羰酰卤制得。
以下的实施例用作本发明更详细的说明以及论证现有技术(对比实施例)。
                    实施例1
                 一般操作步骤
使用表1中列出的烷芳酮类1a至1d的量和图表1中指出的2a至2c的醇量,还有在表1中显示的硫酰氯、二氯甲烷和水的量。确立表1中指定的反应温度。先把1a至1d的烷芳酮引进二氯甲烷和2a至2c中的一种脂族醇类的混合物中,再引入到一个带搅拌的有恒温双套的设备中。所需反应温度已经由带恒温装置的加热和冷却设备来确定。使二氯甲烷中的硫酰氯在1小时期间内计量进搅拌的反应混合物中,同时用自动计量仪器的装置维持反应温度。接着混合物在恒温下搅拌1小时,然后往反应混合物里加水。用有机相的气相色谱分析测定氯化反应的转化率和选择性。
                    图表1
Figure C9610801600071
R1.1     R1.2  R2    R3           R1.1     R1.2  R2    R31a:H        H      H       H  2a:甲醇   3a:H     H     H     H1b:CH3     H      H      H  2b:乙醇   3b:CH3    H     H     H1c:OCH3    H      H      H  2c:异丙醇 3c:OCH3   H     H     H1d:H        H      C2H5 H             3d:H      H     C2H5  H1e:F        H      H      H              3e:F      H     H     H1f:OCH3    OCH3  H      H             3f:OCH3   OCH3  H     H
        表1
   烷芳酮[mmol] 二氯甲烷[ml]      醇[mol]   硫酰氯[mmol]    二氯甲烷[ml]     水[ml]    温度[℃]   转化率[%]    选择性[%]
  1a-100   50   2a-400     140     20     50     20   96.5   >99
  1b-100   50   2a-400     140     20     50     20   95.8   >99
  1c-100   50   2a-400     140     20     50     20   97.3   98.9
  1d-100   50   2a-400     140     20     50     20   >99   97.5
  1e-100   50   2a-400     140     20     50     20   97.8   97.3
  1f-100   50   2a-400     140     20     50     20   97.6   97.1
  1c-100   50   2b-400     140     20     50     20   87.8   96.7
  1c-100   50   2c-400     140     20     50     20   75.1   93.4
  1c-100   50   2a-400     140     20     50     10   >99   94.7
  1c-100   50   2a-400     140     20     50     40   98.6   95.6
  1c-100   50   2a-400     100     20     50     20   67.0   >99
  1c-100   50   2a-400     160     20     50     20   >99   87.6
  1c-100   50   2a-200     140     20     50     20   >99   78.4
  1c-100   50   2a-600     140     20     50     20   91.3   98.5
1)基于烷基酮1
2)基于α-氯烷芳酮3
实施例2(对比实施例,不按本发明的)
采用实例1的一般实验步骤进行表2的对比实验,但不加脂肪醇。编号涉及到图表1。
           表2
  烷基酮[mmol]   二氯甲烷[ml]   醇[mmol]  硫酰氯[mmol]    二氯甲烷[ml]     水[ml]   温度[℃]   转化率1)[%]   选择性2)[%]
  1a-100     50     -    140     20     50     20   >99   76.2
  1b-100     50     -    140     20     50     20   >99   57.0
  1c-100     50     -    140     20     50     20   >99   64.3
1)基于烷芳酮1
2)基于α-氯烷芳酮3

Claims (3)

1.一种制备通式I的α-氯烷芳酮类的方法,
Figure C9610801600021
其中n为1-5,
相互独立的R1为H、烷基、烷氧基、芳基、芳氧基、酰氧基、酰氨基、卤素或硝基,
相互独立的R2,3为H、烷基或芳基,
采用通式II
Figure C9610801600022
的烷基酮类被硫酰氯氯化,其中包括氯化作用要在C1-C4脂肪醇存在下完成。
2.按照权利要求1的方法,其中每摩尔烷芳酮II要使用0.1-10摩尔的醇。
3.按照权利要求1的方法,其中使用的醇是甲醇。
CN96108016A 1995-03-31 1996-03-30 α-氯烷芳酮的制备方法 Expired - Fee Related CN1084725C (zh)

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DE19511861A DE19511861A1 (de) 1995-03-31 1995-03-31 Verfahren zur Herstellung von a-Chloralkylarylketonen
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AU6596800A (en) * 1999-09-03 2001-04-10 Asahi Kasei Kabushiki Kaisha Processes for the preparation of tricyclic amino alcohol derivatives
FR2827602A1 (fr) * 2001-07-23 2003-01-24 Rhodia Chimie Sa Procede de preparation de alpha-halogenoalkylarylcetones et de leurs produits intermediaires halogenes de type cetal cyclique
DE10309645A1 (de) * 2003-03-06 2004-09-16 Basf Ag Verfahren zur Herstellung von a-(3-Arylthio)-acetophenonen
DE10349249A1 (de) * 2003-10-20 2005-05-12 Basf Ag Verfahren zur Herstellung von alpha-(3-Arylthio)-acetophenonen
DE102004024565A1 (de) * 2004-05-18 2005-12-15 Basf Ag Verfahren zur Herstellung von α-Chloralkylpyridylketonen und/oder deren Hydrochloriden
JP5503534B2 (ja) 2007-06-20 2014-05-28 ビーエーエスエフ ソシエタス・ヨーロピア アゾアルクス(Azoarcus)SpEbN1脱水素酵素を用いる光学活性アルコールの製造方法
CA2735769C (en) * 2008-09-17 2018-10-09 Basf Se Method for producing l-phenylephrine using an alcohol dehydrogenase of aromatoleum aromaticum ebn1 (azoarcus sp. ebn1)
WO2013035674A1 (ja) * 2011-09-09 2013-03-14 株式会社クレハ 2-ハロ-1-(1-ハロシクロプロピル)エタノンの製造方法
CN108586220A (zh) * 2018-06-27 2018-09-28 安徽国星生物化学有限公司 一种2-氯-1-(1-氯环丙基)乙酮的合成方法

Citations (3)

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US4328356A (en) * 1979-02-20 1982-05-04 Montedison S.P.A. Process for preparing esters of arylacetic acids from alpha-halo-alkylarylketones
EP0354991A1 (de) * 1988-07-20 1990-02-21 Bayer Ag Verfahren zur Hydrierung von alfa, beta-ungesättigten Ketonen
EP0461483A2 (de) * 1990-06-13 1991-12-18 Bayer Ag Verfahren zur Herstellung von Benzylketonen

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JPH05286902A (ja) * 1992-04-10 1993-11-02 Sumitomo Pharmaceut Co Ltd α−クロロ−β−ケトエステル誘導体の製造方法

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
US4328356A (en) * 1979-02-20 1982-05-04 Montedison S.P.A. Process for preparing esters of arylacetic acids from alpha-halo-alkylarylketones
EP0354991A1 (de) * 1988-07-20 1990-02-21 Bayer Ag Verfahren zur Hydrierung von alfa, beta-ungesättigten Ketonen
EP0461483A2 (de) * 1990-06-13 1991-12-18 Bayer Ag Verfahren zur Herstellung von Benzylketonen

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ATE181724T1 (de) 1999-07-15
CN1142483A (zh) 1997-02-12
CA2172014A1 (en) 1996-10-01
DE19511861A1 (de) 1996-10-02
JPH08277240A (ja) 1996-10-22
DE59602311D1 (de) 1999-08-05
DK0735016T3 (da) 1999-11-22
CA2172014C (en) 2006-01-17

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