摘要
本文以氦为载气,在480~540℃及20~100ml/min 范围内,研究了 H-Y 分子筛催化剂上甲苯歧化反应脉冲动力学,导出了基于表面反应为控速步骤的双分子机理脉冲动力学数学模型,并测定了反应的有关动力学参数.认为,甲苯歧化,在本文实验条件下,是按照双分子吸附的S_N2机理进行.
Pulse kinetics of toluene disproportionation on H-Y zeolite catalyst isstudied within the range of 480~540℃ and 20~100ml/min with helium asthe carrier gas.The mathematical model for the bimolecular mechanismpulse kinetics on the basis of surface reaction acting as rate-limiting stepis derived.As the relative kinetic parameters being determined,we suggestthat toluene disproportionation proceed on the S_(N)2 mechanism of bimolecularabsorption under experiment conditions.
出处
《兰州大学学报(自然科学版)》
CAS
CSCD
北大核心
1990年第2期83-89,共7页
Journal of Lanzhou University(Natural Sciences)
关键词
甲苯
歧化反应
动力学
机理
SN2
toluene disproportionation reaction
reaction kinetics
reaction mechanism
pulse reaction