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。
The calculated results indicate that the highest profit can be gained from a multi-stage adiabatic reactor with radial flow operated under vacuum.
多段绝热反应器在反应过程中需维持温度在最佳温度附近操作。
Multistage insulation reactor in reaction must maintain temperature at aboutoptimum temperature.
采用的固定床绝热反应器和多段反应、段间冷却的工艺是可行的。
It is also feasible to adopt the adiabatic fixed-bed reactor and the techniques of multistage reactions and interstage cooling.
本文对绝热式合成氨反应器，提出一种双线性简化模型。
A bilinear model of adiabatic ammonia reactor has been developed.
给出了8602催化剂于绝热型反应器上的最佳工艺操作条件。
Optimum technological conditions have been provided for 8602catalyst on the adiabatic reactor.
校正后的反应器可分别进行等温操作、绝热操作以及等温和绝热的混合操作，拓宽了仪器适用范围。
As a result, the calibrated reactor could be employed to isothermal operation, adiabatic operation and isothermal-adiabatic operation, which widened the use range of the apparatus.
提出了非绝热式固定床反应器基于改进混合模型的串级非线性推断控制策略。
A new cascade nonlinear inferential control strategy for a nonadiabatic fixed bed reactor based on improved hybrid model is proposed.
非恒温非绝热固定床反应器广泛应用于强放热的反应体系。
The two dimensional pseudohomogeneous model was often used for the non isothermal, non adiabatic fixed bed reactor that was widely used for the strongly exothermic reactions.
采用一维拟均相绝热径向反应器模型模拟乙苯负压脱氢径向反应器。
An one dimensional homogenous adiabatic fixed bed reactor model was adopted to simulate a radial flow reactor for dehydrogenation of ethylbenzene to styrene under vacuum.
采用一维拟均相绝热径向反应器模型模拟乙苯负压脱氢径向反应器。
An one dimensional homogenous adiabatic fixed bed reactor model was adopted to simulate a radial flow reactor for dehydrogenation of ethylbenzene to styrene under vacuum.
应用推荐