合成气一步法5000t/a二甲醚管式反应器设计

Design of tubular reactor for 5 000t/a dimethyl ether directly synthesis from syngas

应用实验所得动力学数据,建立管式固定床反应器的一维数学模型。通过计算典型工况下5000t/a二甲醚反应器,得到了反应器的工艺与设备设计参数。

Based on the fundamental data of kinetics, the one dimensional mathematical model for the tubular reactor with fixed bed is established. The design parameters about technology and equipment of the tubular reactor for 5000t/a dimethyl ether are obtained by calculating the typical industrial instance.