Topology optimization and numerical validation for heat transfer improvement in a packed-bed reactor with monolithic catalyst

被引:2
作者
Erfani, Navid [1 ,4 ]
Symons, Digby [2 ]
Fee, Conan [3 ,4 ]
Watson, Matthew James [1 ,4 ]
机构
[1] Univ Canterbury, Coll Engn, Dept Chem & Proc Engn, Private Bag 4800, Christchurch 4800, New Zealand
[2] Univ Canterbury, Coll Engn, Dept Mech Engn, Private Bag 4800, Christchurch 8041, New Zealand
[3] Univ Canterbury, Sch Prod Design, Private Bag 4800, Christchurch 8041, New Zealand
[4] Univ Canterbury, Biomol Interact Ctr, Private Bag 4800, Christchurch 8041, New Zealand
关键词
Topology optimization; Packed-bed reactor; Monolithic catalyst support; Heat transfer; Steam methane reforming; HYDROGEN-PRODUCTION; GENETIC-ALGORITHMS; DESIGN; PERFORMANCE;
D O I
10.1016/j.cherd.2024.10.012
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study focuses on optimizing heat transfer in packed-bed reactors by simplifying the problem to a twodimensional steady-state heat conduction scenario. The objective is to efficiently arrange a limited volume of high-conductivity material to transport heat from the source to the low-conductivity heat-absorbing materials, representing the reacting fluid phase. The topology optimization problem is tackled using a density-based method that relies on a gradient-based algorithm. The optimized design is extruded and compared to a honeycomb internal structure using high-fidelity simulations for steam methane reforming. Results show a 6.04 % improvement in CH4 conversion for the optimized structure, highlighting the potential of this method to enhance monolithic catalysts, particularly in cases where heat transfer critically influences the reaction.
引用
收藏
页码:212 / 220
页数:9
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