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摘要：In this paper, the numerical simulation of bubbling reactor was carried out under the condition of the amplification design of chlorine dissolving bubbling reactor in the epoxy propane chlorohydrin production process. The gas hold-up and flow field distribution in a side-entry bubbling reactor were studied. The simulation results show that the side-entry bubbling reactor can intensify the fluid disturbance near the wall so that the gas substance can contact with the liquid fully and the reaction time can also be increased. Hence, the mass transfer between the gas-liquid two phases was enhanced.

卷号：1

期号：1064

是否译文：否