Synthesis method of alpha phenyl ethanol
A synthesis method and technology of phenylethyl alcohol, applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problems of easy environmental pollution, low synthesis selectivity, complicated operation, etc., and achieve high utilization rate , high product selectivity and simple process
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Embodiment 1
[0022] Add 2.5g of Raney nickel catalyst (3.4mL bulk volume) in the fixed-bed reactor, the ratio of the amount of acetophenone, methanol, water substance is 1: 15: 20 mixed liquid with the liquid hourly space velocity being 0.706 hours -1Add it into the reactor, adjust the reaction temperature to 120°C, and the reaction pressure to 0.4MPa. The product at the outlet of the reactor is separated from the liquid product by a gas-liquid separator. The conversion rate of ethyl ketone is 36.59%, the selectivity of α-phenylethanol is 83.81%, and the selectivity of by-product ethylbenzene is 16.19%.
Embodiment 2
[0024] Add 2.5g of Raney nickel catalyst (3.4mL bulk volume) in the fixed-bed reactor, the ratio of the amount of acetophenone, methanol, water substance is 1: 15: 20 mixed liquid with the liquid hourly space velocity being 0.706 hours -1 Add it into the reactor, adjust the reaction temperature to 130°C, and the reaction pressure to 0.52MPa. The product at the outlet of the reactor is separated from the liquid product by a gas-liquid separator, and the liquid product is analyzed by Agilent-GC-MS. The conversion rate of ethyl ketone was 40.41%, the selectivity of α-phenylethanol was 90.35%, and the selectivity of by-product ethylbenzene and α-cyclohexyl alcohol were 9.09% and 0.56%, respectively.
Embodiment 3
[0026] Add 2.5g of Raney nickel catalyst (3.4mL bulk volume) in the fixed-bed reactor, the ratio of the amount of acetophenone, methanol, water substance is 1: 15: 20 mixed liquid with the liquid hourly space velocity being 0.706 hours -1 Add it into the reactor, adjust the reaction temperature to 140 ° C, and the reaction pressure to 0.7 MPa. The product at the outlet of the reactor is separated from the liquid product by a gas-liquid separator. The conversion rate of ethyl ketone is 47.59%, the selectivity of α-phenylethanol is 77.35%, and the selectivity of by-product ethylbenzene, α-cyclohexyl ethanol, cyclohexyl ethyl ketone and cyclohexyl ethane are 22.06%, 0.29% respectively , 0.20% and 0.11%.
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