摘要
在内循环无梯度反应器内研究了C6H12-H2O转化反应的宏观动力学(实验条件:常压;温度460～570 ℃;H2O/C3.0,4.0,5.0)。并用Pow
Macro kinetics of cyclic hydrocarbon steam reforming was studied in an internal recycle gradientless reactor under atmospheric pressure, steam carbon reactions at 3,4,5 (mol/mol) and temperature 460~570℃. The reaction rate equation not only could simulate the process of cyclohexane steam reforming reaction, but also can be used to predict the variation of products composition.
出处
《青岛大学学报（工程技术版）》
CAS
1999年第4期16-18,共3页
Journal of Qingdao University(Engineering & Technology Edition)
关键词
环烷烃
水蒸汽转化
速率方程
cyclic hydrocarbon
water gas shift
rate equation
