Technique of synthesizing ethanol with acetic acid
A technology of ethyl acetate and acetic acid, which is applied in the field of ethanol production from acetic acid, can solve the problems of low conversion rate of acetic acid and incomplete conversion of acetic acid, and achieve the effect of overcoming low conversion rate
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Embodiment 1
[0023] Process flow of the present invention such as figure 1 Shown, acetic acid enters esterification reactor 1 through pipeline 1, reacts with crude ethanol from pipeline 9 under the effect of acidic catalyst to generate ethyl acetate product, and the product containing ethyl acetate of generation enters crude separation tower through pipeline 2 II. In the crude separation tower, the unreacted acetic acid is separated, and then returned to the esterification reactor I through the pipeline 4. The crude ester containing ethyl acetate separated from the crude fractionation column enters the vaporization tower III through the pipeline 3. In the vaporization tower III, the crude ester from the pipeline 3 is mixed with hydrogen and heated to the bubble point of the crude ester, and then passed through the pipeline 5 It enters the hydrogenation reactor IV and reacts under the action of a copper-based catalyst. The reacted stream mainly contains ethanol, water, unreacted hydrogen, a...
Embodiment 2
[0025] The temperature of reaction in embodiment 1 is changed into 180 o C, the reaction pressure becomes 0.5 MPa, the molar ratio of hydrogen and ethyl acetate is 100, the selectivity of reaction result ethanol is 98.2%, the space-time yield of ethanol is 412.7 g kg -1 h -1 .
Embodiment 3
[0027] The temperature of reaction in embodiment 1 is changed into 300 o C, the reaction pressure becomes 5.0 MPa, the molar ratio of hydrogen to ethyl acetate is 10, the selectivity of the reaction result ethanol is 95.3%, the space-time yield of ethanol is 1633.6 g kg -1 h -1 .
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