This paper expounds the selection of the catalyst of the. synthetic reaction of dimethyl sulfide and the calculation of the loading height of the catalyst in the reactor.
阐述了二甲基硫醚合成反应所用催化剂的选择和反应器中催化剂装填高度的计算。
2
The volumetric exchange rate of feeding and draining simultaneously in the reactor can reach 65-74% if only the influent hydraulic loading rate is controlled properly.
只要适当控制进水水力负荷，反应器的同时进出水体积置换率可达65-74％。
3
The details of dynamic response analysis for reactor and steam generator under LOCA and seismic loading were performed.