A Study on the Macro-Kinetics of Methane-Steam Reforming Reaction with Wheel Catalysts 车轮形催化剂上甲烷水蒸汽转化反应宏观动力学的研究
The macro-kinetics of methane-steam catalytic reforming reaction with wheel catalysts of original sizes was investigated in an internal recycling gradientless reactor ( Type KD-1) under 3.04 × 106 Pa absolute pressure. 在3.04×10~6Pa压力下使用KD-1型内循环式无梯度反应器研究了原粒度七筋车轮形催化剂上甲烷水蒸汽催化转化反应的宏观动力学。