thermal reactor

The research of ethylbenzene dehydrogenation kinetics has been carried out in an experimental adiabatic reactor.

在实验室绝热反应器中进行了乙苯脱氢制苯乙烯的反应动力学研究。

First, the nature of dehydrogenation of ethylbenzene to styrene was studied in an experilmen-tal adiabatic reactor.

针对乙苯脱氢绝热反应器工程特点建立了有关转化率和选择性的数学模型。

Based on the said principle,a mathematical model of an exothermic reactor(ammonia sythesis reactor)has been established,the influence of reactor s inlet gas temperature and reactant s flow rate upon the ammonia synthesis reaction under condition of definite designed pre.

介绍了氨基热化学储能的基本原理,在此基础上建立了放热反应器(氨合成反应器)的数学模型,定量分析和讨论了在一定设计压力和氢氮比条件下,进气温度和进气流率对反应的影响,给出了实现火用最优化和热能最大化的操作参数,并比较了最优火用和最大热能的关系。

Based on this principle,a mathematical model of an exothermic reactor(ammonia-synthesizing reactor) is established to obtain the curves of the exothermic reactor length versus the reaction temperature,of the reaction temperature versus the molar fraction of ammonia and of th.

文中分析了储能体系的选择,介绍了氨基热化学储能的基本原理,在此基础上建立了放热反应器(氨合成反应器)的数学模型,计算和绘制出了放热反应器长度与反应温度、反应温度与氨摩尔分数以及热量和输出与反应器内壁平均温度之间的关系曲线,直观地反映了在一定的设计压力和氢氮比下,进气温度和进气流率对放热反应的影响,给出了实现最优化和热能最优化的操作参数。