Mechanistic Insights into the Induction Period of Methanol-to-Olefin Conversion over ZSM-5 Catalysts: A Combined Temperature-Programmed Surface Reaction and Microkinetic Modeling Study

被引:3
|
作者
Omojola, Toyin [1 ,2 ]
机构
[1] Univ Bath, Dept Chem Engn, Bath BA2 7AY, England
[2] Chalmers Univ Technol, Dept Mech & Maritime Sci, Div Fluid Dynam, SE-41296 Gothenburg, Sweden
关键词
CARBON-CARBON BOND; DIMETHYL ETHER; ZEOLITE H-ZSM-5; HYDROCARBON FORMATION; METHOXY GROUPS; KINETIC-MODEL; O-COMPOUNDS; HZSM-5; INITIATION; DENSITY;
D O I
10.1021/acs.iecr.3c01401
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The induction period of propylene formation from methanol is compared to that of dimethyl ether (DME) over ZSM-5 catalysts of different compositions using a combination of temperature-programmed surface reaction experiments and microkinetic modeling. Transient reactor performance is simulated by solving coupled 1D nonlinear partial differential equations accounting for elementary steps based on the methoxy methyl mechanism and axial dispersion and convection in the reactor. Three binding site ensembles and three active site ensembles are observed. These sites constitute up to 3% (binding sites similar to 70%, active sites similar to 30%) of the total acid sites during methanol conversion and up to 1% (binding sites similar to 30%, active sites similar to 70%) of the total acid sites during DME conversion. Over the binding sites, during the induction period of methanol, and DME conversion, the acid site density is the key descriptor. Over the active sites, acid site density is the key descriptor with higher site densities correlating with lower barriers of propylene formation during the induction period of methanol conversion. The barrier to DME desorption is the key descriptor, with lower desorption barriers correlating with lower barriers of propylene formation during the induction period of DME conversion. Barriers to propylene formation are lower during the induction period of methanol conversion (up to 141 kJ mol(-1)) compared to that of DME conversion (up to 200 kJ mol(-1)) over ZSM-5 catalysts.
引用
收藏
页码:14244 / 14265
页数:22
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