Jerzy Szczygie?, Marek Stolarski. Mathematical analysis of physicochemical phenomena in the catalyst during hydrogenating depolymerization of coal extract benzene insoluble fraction[J]. 中国化学工程学报(英文版), 2015,(6):962-973.
Jerzy Szczygie?, Marek Stolarski. Mathematical analysis of physicochemical phenomena in the catalyst during hydrogenating depolymerization of coal extract benzene insoluble fraction[J]. Chinese Journal of Chemical Engineering, 2015, (6): 962-973.
Jerzy Szczygie?, Marek Stolarski. Mathematical analysis of physicochemical phenomena in the catalyst during hydrogenating depolymerization of coal extract benzene insoluble fraction[J]. 中国化学工程学报(英文版), 2015,(6):962-973.DOI: 10.1016/j.cjche.2014.08.008.
Jerzy Szczygie?, Marek Stolarski. Mathematical analysis of physicochemical phenomena in the catalyst during hydrogenating depolymerization of coal extract benzene insoluble fraction[J]. Chinese Journal of Chemical Engineering, 2015, (6): 962-973.DOI: 10.1016/j.cjche.2014.08.008.
Mathematical analysis of physicochemical phenomena in the catalyst during hydrogenating depolymerization of coal extract benzene insoluble fraction
Efficiency and selectivity of hydrogenating depolymerization of the coal extract benzene-insoluble part over the heterogeneous Co–Mo/Al
2
O
3
catalystwere assessed us
ing a mathematical model. The analytical equations of the mathematical modelwere generated based onmaterial balance incorporating the physico-chemical phenomena (reaction and diffusion) both in the autoclave and the catalyst grain. The equations offer the possibility for predicting changes of the reactants in the autoclave during the process and for determining the distribution of reactant concentrations in the grain as a function of its radius. The analytical equations of the model serve as the basis of the algorithm for assessing the influence of restrictive diffusion on the effectiveness and selectivity of the catalyst
and also for defining the optimal radii of the catalyst's pores to enable free transport of reactants in the grain interior.
Abstract
Efficiency and selectivity of hydrogenating depolymerization of the coal extract benzene-insoluble part over the heterogeneous Co-Mo/Al
2
O
3
catalystwere assessed using a mathematical model. The analytical equations of the mathematical modelwere generated based onmaterial balance incorporating the physico-chemical phenomena (reaction and diffusion) both in the autoclave and the catalyst grain. The equations offer the possibility for predicting changes of the reactants in the autoclave during the process and for determining the distribution of reactant concentrations in the grain as a function of its radius. The analytical equations of the model serve as the basis of the algorithm for assessing the influence of restrictive diffusion on the effectiveness and selectivity of the catalyst
and also for defining the optimal radii of the catalyst's pores to enable free transport of reactants in the grain interior.
关键词
Keywords
references
The trial reading is over, you can activate your VIP account to continue reading.
Reaction pathways and selectivity in the chemo-catalytic conversion of cellulose and its derivatives to ethylene glycol: A review
A Ruddlesden–Popper oxide as a carbon dioxide tolerant cathode for solid oxide fuel cells that operate at intermediate temperatures
A review of conventional and renewable biodiesel production
Promotion effect of Re additive on the bifunctional Ni catalysts for methanation coupling with water gas shift of biogas: Insights from activation energy
Ethylbenzene disproportionation and p-xylene selectivity enhancement in xylene isomerization using high crystallinity desilicated H-ZSM-5
相关作者
Yao Li
Yuchun Zhang
Zhiyu Li
Huiyan Zhang
Peng Fu
Shujun Peng
Song Lei
Sisi Wen
相关机构
College of Agricultural Engineering and Food Science, Shandong University of Technology
Key Laboratory of Energy Thermal Conversion and Control, Ministry of Education, School of Energy and Environment, Southeast University
School of Chemistry & Chemical Engineering, Jinggangshan University
School of Chemistry & Chemical Engineering, Guangdong Provincial Key Lab of Green Chemical Product Technology, South China University of Technology
Beijing Key Laboratory of Membrane Materials and Engineering, Department of Chemical Engineering, Tsinghua University