Modelling and simulation of the flux responses of a gas-solid catalytic micro-reactor

Chemical Engineering Science

Volumn 57, Issue 6, 2002, Pages 953-966

  Buffham, B A ^a   Hellgardt, K ^a   Heslop, M J ^a   Mason, G ^a   Richardson, D J ^a  

^a LOUGHBOROUGH UNIVERSITY   (United Kingdom)

Author keywords

Adsorption; Catalysis; Flux response; Micro reactor; Reaction engineering; Transient response

Indexed keywords

ADSORPTION; CHEMICAL REACTORS; COMPUTER SIMULATION; DESORPTION; MAGNETIC FLUX; MATHEMATICAL MODELS; SIMULATORS;

GAS-SOLID CATALYTIC MICRO-REACTORS;

CATALYSTS;

ABSORPTION; CATALYST; GAS-SOLID SEPARATION; MEASUREMENT METHOD; MODELING; REACTOR;

EID: 0037075490     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0009-2509(01)00436-5     Document Type: Article

References (40)

1. Effects of pore-level reaction on dispersion in porous media
2. Über Erwärmung vermittels durchströmender Medien
3. Communications on the theory of diffusion and reaction - IX. Internal pressure and forced flow for reactions with volume change
4. The concentration factor in vapour phase partition chromatography
5. Sorption-effect chromatography
6. Absolute gas chromatography
7. Remote sensing of the flux responses of a gas-solid catalytic micro-reactor
8. Applications of EPR to a study of the hydrogenation of ethene and benzene over a supported Pd catalyst - Detection of free radicals on a catalyst surface
9. Dynamic Monte-Carlo and mean-field study of the effect of strong adsorption sites on self-diffusion in zeolites
10. A mathematical models for dispersion in the direction of flow in porous media
11. A computational model for predicting and correlating the behavior of fixed bed reactors. 1. Derivation of model for non-reactive systems
12. A computational model for predicting and correlating the behavior of fixed bed reactors. II. Extension to chemically reactive systems
13. Maxwell-Stefan analysis of multicomponent transient diffusion in a capillary and adsorption of hydrocarbons in activated carbon particle
14. 2
15. 2
16. Gravimetric transient response study of adsorption and reaction of propylamines on alumina
17. Residence time distribution function for multistage systems with backmixing
18. Models of pore diffusion in porous catalysts
19. An improved linear driving force approximation for intraparticle adsorption
20. Single phase flow modelling in packed beds: Discrete cell approach revisited
21. The generalized Maxwell-Stefan model for diffusion in zeolites: Sorbate molecules with different saturation loadings
22. Effect of sorbate-sorbate interaction on micropore diffusion in steady-state adsorption processes
23. On hydrodynamic mixing in a model of a porous medium with stagnant zones
24. Gas adsorption isotherms from composition and flowrate transient times in chromatographic columns, I. Basic theory and a binary experimental test
25. Gas adsorption isotherms from composition and flowrate transient times in chromatographic columns, II. Effect of pressure changes
26. Gas adsorption isotherms from composition and flowrate transient times in chromatographic columns, III. Effect of gas viscosity changes
27. A non-isothermal, non-equimolar transient kinetic model for gas-solid reactions
28. Determination of the volumes of void zones in packed chromatographic columns
29. Transient response and moments analysis of backflow cell model for flow systems with longitudinal mixing
30. 2
31. Residence-time distribution in systems with internal reflux
32. Fixed-bed adsorption of two linearly adsorbed components in the presence of an inert
33. Effect of fluid dispersion coefficients on particle-to-fluid mass transfer coefficients in packed beds. Correlation of sherwood numbers
34. Maxwell-Stefan theory for macropore molecular-diffusion-controlled fixed-bed adsorption