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公开(公告)号:US20150246864A1
公开(公告)日:2015-09-03
申请号:US14709948
申请日:2015-05-12
Applicant: BASF SE
Inventor: Rudolf Schuch , Stefan Rüdenauer , Klaus Ebel , Ralf Pelzer , Andreas Keller
CPC classification number: C07C29/44 , B01J21/08 , B01J23/462 , B01J23/56 , B01J33/00 , B01J35/0026 , B01J35/008 , B01J35/023 , B01J35/08 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/108 , B01J37/0203 , B01J37/18 , C07C29/19 , C07C29/80 , C07C2601/14 , C11B9/0061 , C07C33/20 , C07C31/1355
Abstract: A process for preparing 4-cyclohexyl-2-methyl-2-butanol, comprising: a) reaction of styrene with isopropanol at elevated temperature to obtain 2-methyl-4-phenyl-2-butanol, and b) heterogeneously catalyzed hydrogenation of 2-methyl-4-phenyl-2-butanol over a catalyst suitable for ring hydrogenation of aromatics, where the molar ratio of the styrene used in step a) to the isopropanol used in step a) is in the range from 1:below 5 to 1:0.5.
Abstract translation: 一种制备4-环己基-2-甲基-2-丁醇的方法,包括:a)在升高的温度下使苯乙烯与异丙醇反应得到2-甲基-4-苯基-2-丁醇,和b)异构催化氢化2 - 甲基-4-苯基-2-丁醇,其适用于芳族化合物的环加氢,其中步骤a)中使用的苯乙烯的摩尔比与步骤a)中使用的异丙醇的摩尔比在1:低于5至 1:0.5。
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公开(公告)号:US09416079B2
公开(公告)日:2016-08-16
申请号:US14709948
申请日:2015-05-12
Applicant: BASF SE
Inventor: Rudolf Schuch , Stefan Rüdenauer , Klaus Ebel , Ralf Pelzer , Andreas Keller
IPC: C07C33/18 , C07C29/44 , C07C29/19 , C07C29/80 , B01J23/46 , B01J23/56 , B01J35/10 , B01J37/18 , B01J21/08 , B01J33/00 , B01J35/00 , B01J35/02 , B01J35/08 , B01J37/02
CPC classification number: C07C29/44 , B01J21/08 , B01J23/462 , B01J23/56 , B01J33/00 , B01J35/0026 , B01J35/008 , B01J35/023 , B01J35/08 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/108 , B01J37/0203 , B01J37/18 , C07C29/19 , C07C29/80 , C07C2601/14 , C11B9/0061 , C07C33/20 , C07C31/1355
Abstract: A process for preparing 4-cyclohexyl-2-methyl-2-butanol, comprising: a) reaction of styrene with isopropanol at elevated temperature to obtain 2-methyl-4-phenyl-2-butanol, and b) heterogeneously catalyzed hydrogenation of 2-methyl-4-phenyl-2-butanol over a catalyst suitable for ring hydrogenation of aromatics, where the molar ratio of the styrene used in step a) to the isopropanol used in step a) is in the range from 1:below 5 to 1:0.5.
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