adiabatic reactor

基本解释

Optimum technological conditions have been provided for 8602catalyst on the adiabatic reactor.
给出了8602催化剂于绝热型反应器上的最佳工艺操作条件。
The diameter of a fixed-bed adiabatic reactor, height of catalyst bed and catalyst loading were calculated by using Runge-Kutta numerical solution method.
采用龙格-库塔数值解法，计算了不同设计方案时，固定床绝热反应器的直径、催化剂床层高度及装量；
The calculated results indicate that the highest profit can be gained from a multi-stage adiabatic reactor with radial flow operated under vacuum.
计算结果表明，负压操作的多段径向绝热反应器所获收益最高。