Effects of catalyst amount, membrane tube diameter and permeation rate on the performance of porous membrane reactors

Journal of Chemical Engineering of Japan

Volumn 34, Issue 11, 2001, Pages 1332-1340

  Trianto, Azis ^a   Kokugan, Takao ^b  

^a BANDUNG INSTITUTE OF TECHNOLOGY   (Indonesia)

^b TOKYO UNIVERSITY OF AGRICULTURE AND TECHNOLOGY   (Japan)

Author keywords

Cyclohexane dehydrogenation; Equilibrium shifting; Membrane reactor; Organic separation; Reactor modeling

Indexed keywords

CATALYSTS; COMPUTER SIMULATION; MEMBRANES; POROUS MATERIALS;

MODIFIED POROUS MEMBRANE REACTORS (MPMR);

CHEMICAL REACTORS;

CATALYST; GLASS MEMBRANE; MEMBRANE TECHNOLOGY; PERMEATION;

CATALYST; CONCENTRATION (PARAMETERS); EXPERIMENT; MEMBRANE REACTOR; PERFORMANCE; PERMEABILITY; POROSITY; SIMULATION;

EID: 0035517121     PISSN: 00219592     EISSN: None     Source Type: Journal    
DOI: 10.1252/jcej.34.1332     Document Type: Article

References (10)

1. Application of catalytic inorganic membrane reactors to refinery products
2. A membrane reactor using palladium
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4. Catalytic reactor with porous membrane: Apparatus and procedure for chemicals production
5. Dehydrogenation of pure cyclohexane in the membrane reactor and prediction of conversion by pseudo equilibrium model
6. Dehydrogenation of isobutane to isobutene in a palladium membrane reactor
7. Gas diffusion in microporous media in Knudsen's regime
8. Method for improving the performance of porous membrane reactor
9. A novel method for improving the performance of porous membrane reactor fed with pure reactant
10. Dehydrogenation of cyclohexane on a hydrogen-porous membrane