Micro-kinetics analysis based on partial reaction networks to compare catalysts performances for methane dry reforming reaction

被引:1
|
作者
Shambhawi [1 ]
Weber, Jana M. [2 ]
Lapkin, Alexei A. [1 ,3 ]
机构
[1] Univ Cambridge, Dept Chem Engn & Biotechnol, Cambridge, England
[2] Delft Univ Technol, Intelligent Syst Dept, Delft, Netherlands
[3] CARES Ltd, Cambridge Ctr Adv Res & Educ Singapore, 1 Create Way, Singapore, Singapore
基金
英国工程与自然科学研究理事会; 新加坡国家研究基金会;
关键词
CO 2 reforming of methane; Reaction Network; Catalyst design; Heterogeneous catalysis; Catalyst descriptors; Network accumulation and congestion; GAS SHIFT REACTION; ASSISTED MICROKINETIC ANALYSIS; RATE EXPRESSION; NI; CARBON; MODEL; MECHANISMS; PATHWAYS; STEAM; TOOL;
D O I
10.1016/j.cej.2023.143212
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
Designing a simple, yet representative reaction network for subsequent micro-kinetic analysis is important for limiting the cost of evaluation and ensuring model solvability. This is currently achieved by employing sensitivity analysis over a comprehensive reaction network (CRN) to screen reaction species. However, as a reaction network is being simplified for a particular catalyst composition, it loses its transferability to other compositions. Therefore, in this study, a two-way approach is presented to circumvent this problem. Firstly, a generalizable model outcome is identified, i.e. minimum reactant conversions (xR), based on a mass-flow analysis. Then, a stepwise workflow is developed for constructing a partial reaction network (PRN) to insure transferability of min (xR) for a range of varying catalyst energetics, in the absence of experimental data for validation. Lastly, the transferability of this approach is demonstrated for CH4 dry reforming by developing a PRN using Ni(1 1 1) as the initial catalyst and testing it over Ru(0 0 1).
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页数:14
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