Dimensionless analysis of reverse water gas shift Packed-Bed membrane reactors

被引:3
|
作者
Dzuryk, Stephen [1 ]
Rezaei, Ebrahim [1 ]
机构
[1] Lakehead Univ, Dept Chem Engn, Thunder Bay, ON P7B 5E1, Canada
关键词
Syngas production; Reverse water gas shift reaction; Intensification; Dimensionless analysis; H2O-permeable membranes; CO2; CONVERSION; CATALYSTS; STEAM;
D O I
10.1016/j.ces.2021.117377
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A dimensionless analysis was performed on the reverse water gas shift packed-bed membrane reactors (RWGS PBMRs) to shift the equilibrium of the RWGS reaction by in-situ H2O removal at low temperatures. Using Damkohler, Peclet, and Stanton dimensionless numbers, the effects of sweep to reactor flow and pressure ratios, flow configuration, temperature, and H2O/H2 perm-selectivity were studied for CuO/ZnO/Al2O3 and Ru-Cu/ZnO/Al2O3 catalysts. The counter-current configuration resulted in higher CO2 conversions at milder sweep pressures when compared to the co-current configuration. It was determined that the application of RWGS PBMRs had to be limited to temperatures below 300 degrees C to shift the reaction equilibrium. It was concluded that to meaningfully intensify the RWGS reaction by PBMRs, weight hourly space velocities should be lowered to values below 1 hr-1 using membranes with H2O/ H2 perm-selectivities greater than 100 and H2O permeance in the range of 10-6-10-5 mol m-2 s-1 Pa-1. (c) 2021 Elsevier Ltd. All rights reserved.
引用
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页数:16
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