An Experimental and Kinetic Modelling Study for Methane Oxidation over Pd-based Catalyst: Inhibition by Water

An Experimental and Kinetic Modelling Study for Methane Oxidation over Pd-based Catalyst:... d Hydraulic diameter of the channel (m) hyd E Activation energy for reaction i (J/mol) A,i −1 GSA Geometric surface area per reactor volume (m ) Gz The Graetz number for mass transfer mass −1 k Rate constant for reaction i (s ) k Mass transfer coefficient of species k (mol/m s) k,m MG Molar mass of gas phase species k (kg/kmol) k,g r Reaction rate for reaction i (kmol/(m s)) Re The Reynolds number Sc The Schmidt number Sh The Sherwood number T Temperature at catalyst surface (K) t Time (s) v Gas velocity (m/s) v Stoichiometric coefficient of species k in reaction i i,k (−) * Louise Olsson w Mass fraction of species k in gas phase (−) k,g y Mole fraction at the reaction layer of species k (−) y Mole fraction in the gas bulk of specie k (−) Chemical Engineering, Competence Centre for Catalysis, Chalmers University of Technology, 412 96 Gothenburg, z Spatial coordinate in axial direction (m) Sweden Johnson Matthey AB, 421 31 Västra Frölunda, Sweden Greek Symbols Coverage dependence in reaction i (−) Scania CV AB, 151 87 Södertälje, Sweden Monolith wall thickness (μm) wall AVL MTC Motortestcenter AB, P. O. Box 223, Monolith washcoat thickness (μm) 13623 Haninge, Sweden wc Vol:.(1234567890) Catalysis Letters Springer Journals

An Experimental and Kinetic Modelling Study for Methane Oxidation over Pd-based Catalyst: Inhibition by Water

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Springer US
Copyright © 2017 by The Author(s)
Chemistry; Catalysis; Industrial Chemistry/Chemical Engineering; Organometallic Chemistry; Physical Chemistry
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