2017
DOI: 10.1103/physreve.96.022115
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Particle-based modeling of heterogeneous chemical kinetics including mass transfer

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Cited by 8 publications
(9 citation statements)
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“…Due to the fast acid–base interaction between QNNH 2 and attached SO 3 H, the loading capacity of QNNH 2 mainly depends on the adsorptive flux (or reactive flux J R ) of QNNH 2 in the shells. According to the ever-reported theoretical research, , the reactive flux and adsorption rate constant are given as Combining eqs and leads to Where m is the mass of component, k B T is energy, p on is the probability that a striking particle sticks, A cat is the total area of catalyst, N cat is the number of catalytic sites, and θ vac is the fractional vacancy of catalytic sites at steady state. In the immobilization of QNNH 2 via fast acid–base reaction, the number of total acid site (SO 3 H) ( N cat ) is obtained by the content of sulfur from elemental analysis.…”
Section: Resultsmentioning
confidence: 99%
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“…Due to the fast acid–base interaction between QNNH 2 and attached SO 3 H, the loading capacity of QNNH 2 mainly depends on the adsorptive flux (or reactive flux J R ) of QNNH 2 in the shells. According to the ever-reported theoretical research, , the reactive flux and adsorption rate constant are given as Combining eqs and leads to Where m is the mass of component, k B T is energy, p on is the probability that a striking particle sticks, A cat is the total area of catalyst, N cat is the number of catalytic sites, and θ vac is the fractional vacancy of catalytic sites at steady state. In the immobilization of QNNH 2 via fast acid–base reaction, the number of total acid site (SO 3 H) ( N cat ) is obtained by the content of sulfur from elemental analysis.…”
Section: Resultsmentioning
confidence: 99%
“…Theoretically, the mass transport processes in a porous slab and a porous sphere, coupled with convection and reaction kinetics, were thoroughly discussed. For the first order kinetics, the effectiveness factor (η), introduced to take account of the influence of pore diffusion on reaction rate, is given as a function of Thiele modulus for spherical particle in the case of constant concentration at the surface where ϕ s is the Thiele modulus for a sphere, k 1 is first-order kinetic constant (s –1 ), R is the sphere radius (cm), and D e is the effective diffusion coefficient (cm 2 s –1 ). Based on eqs and , the more effective diffusion coefficient ( D e ) and shorter sphere radius ( R ) are favorable for achieving better effectiveness factor (η).…”
Section: Introductionmentioning
confidence: 99%
“…To implement heterogeneous chemical reactions, the Langmuir adsorption-reaction model proposed by Sengar [55] is applied. Details of the model can be found in Appendix.…”
Section: Temperature Programed Desorption and Isothermal Surface Reactionsmentioning
confidence: 99%
“…In this work we use the reaction method suggested by Sengar [55]. When a SRD particle bounces on a catalytic surface, the particle will be adsorbed with a certain probability p a .…”
Section: Appendix: Simulating Heterogeneous Reactionsmentioning
confidence: 99%
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