4-(3-甲基丁-2-烯基)苯酚

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 85 g 4-(3-methyl-but-2-enyl)-phenol, 3 wt. % rhodium-on-active charcoal (Rh content, based on the weight of the dry catalyst: 5%; wafer content about 50%) are initially introduced into 300 ml cyclohexane in a stirred autoclave with a gassing stirrer. Hydrogenation is carried out for 5 hours at 100° C. under a hydrogen pressure of 20 bar. After filtration, 85 g 4-isoamylcyclohexanol are obtained as a crude product. After distillation, 80 g 4-isoamylcyclohexanol, which has the following composition: 50.4% cis-4-isoamylcyclohexanol and 49.1% trans-4-isoamylcyclohexanol, are obtained. After filtration, 85 g 4-isoamylcyclohexanol are obtained as a crude product After distillation, 80 g 4-isoamylcyclohexanol, which

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 85 g 4-(3-methyl-but-2-enyl)-phenol, 3 wt % rhodium-on-active charcoal (Rh content, based on the weight of the dry catalyst: 5%; water content about 50%) are initially introduced into 500 ml isopropanol and 9.6 g methanesulfonic acid in a stirred autoclave with a gassing stirrer. Hydrogenation is carried out for 5 hours at 80° C. under a hydrogen pressure of 10 bar. After filtration, 85 g 4-isoamylcyclohexanol are obtained as a crude product. After distillation, 80 g 4-isoamylcyclohexanol, which has the following composition: 67.6% cis-4-isoamylcyclohexanol and 31.8% trans-4-isoamylcyclohexanol, are obtained. After filtration, 85 g 4-isoamylcyclohexanol are obtained as a crude product After distillation, 80 g 4-isoamylcyclohexanol, which

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 330 g 4-(3-methyl-but-2-enyl)-phenol, 3 wt. % ruthenium-on-active charcoal (Ru content, based on the weight of the dry catalyst: 5%; water content about 50%) are initially introduced into 570 ml isopropanol in a stirred autoclave with a gassing stirrer. Hydrogenation is carried out for 5 hours at 100° C. under a hydrogen pressure of 130 bar. After filtration, 329 g 4-isoamylcyclohexanol are obtained as a crude product. After distillation, 316 g 4-isoamylcyclohexanol, which has the following composition: 53.8% cis-4-isoamylcyclohexanol and 44.9% trans-4-isoamylcyclohexanol, are obtained. After filtration, 329 g 4-isoamylcyclohexanol are obtained as a crude product After distillation, 316 g 4-isoamylcyclohexanol, which

反应条件: temp:0.00; pressure:0.00; stir:; See reaction.notes.procedure_details.

实验步骤: 165 g 4-(3-methyl-but-2-enyl)-phenol, 2 wt. % Raney nickel-iron (composition of the catalyst: 45% nickel, 3% aluminium, 8% iron; water content 44%) are initially introduced into a stirred autoclave with a gassing stirrer. Hydrogenation is carried out for 6 hours at 170° C. under a hydrogen pressure of 20 bar. After filtration, 165 g of crude product are obtained. 158 g 4-isoamylcyclohexanol (b.p.: 65° C., 0.6 mbar), which has the following composition: 33.1% cis-4-isoamylcyclohexanol and 66.3% trans-4-isoamylcyclohexanol, are obtained by distillation of the crude product. After filtration, 165 g of crude product are obtained