Process for synthesizing isopropyl acetate and method for preparing its catalyst
A technology of isopropyl acetate and synthesis process, which is applied in the direction of catalyst activation/preparation, carboxylic acid ester preparation, organic compound preparation, etc., can solve the problems of many side reactions, high production costs, high equipment investment and maintenance costs, and achieve High activity and selectivity, reduced production cost, and the effect of overcoming equipment corrosion
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Embodiment 1
[0015] Put 2ml of HD-1 modified resin catalyst into the above-mentioned reaction tube, adjust the reaction temperature to 125°C, activate the catalyst with nitrogen for 8 hours, turn on the micro feed pump and feed at a rate of 2.2ml per hour for 15 minutes Finally, start to feed propylene, and after replacing the air under normal pressure, gradually increase the pressure to 1.0Mpa. To promote the reaction, keep the tail propylene flow rate at 30ml / min. The reaction can be sampled and analyzed after a period of time (6-8 hours). The product was analyzed by Shimadzu GC-7A gas chromatograph, the conversion rate of acetic acid was 90%, and the selectivity of the generated isopropyl acetate was 99.1%.
Embodiment 2
[0017] HD-1 type modified resin catalyst has been carried out life test according to the condition described in embodiment 1, and continuous operation 1000 hours, catalyst activity drops to about 42% from 90%, the selectivity of the isopropyl acetate of generation is 99% %.
Embodiment 3
[0019] Except that the reaction temperature is changed to 95° C., the others are the same as in Example 1, and the result is: the conversion of acetic acid is 80%, and the selectivity of isopropyl acetate is 99.0%.
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