adiabatic reactor

基本解釋

Optimum technological conditions have been provided for 8602catalyst on the adiabatic reactor.
給出了8602催化劑于絕熱型反應器上的最佳工藝操作條件。
The diameter of a fixed-bed adiabatic reactor, height of catalyst bed and catalyst loading were calculated by using Runge-Kutta numerical solution method.
采用龍格-庫塔數(shù)值解法，計算了不同設(shè)計方案時，固定床絕熱反應器的直徑、催化劑床層高度及裝量；
The calculated results indicate that the highest profit can be gained from a multi-stage adiabatic reactor with radial flow operated under vacuum.
計算結(jié)果表明，負壓操作的多段徑向絕熱反應器所獲收益最高。