Comparison of the catalytic performance of V2O5/γ-Al2O3 in the oxidehydrogenation of propane to propylene in different reactor configurations: I packed-bed reactor, ii monolith-like reactor and iii catalytic membrane reactor

Chemical Engineering Science

Volumn 51, Issue 10, 1996, Pages 1817-1826

  Capannelli, G ^a   Carosini, E ^a   Cavani, F ^b   Monticelli, O ^a   Trifiro, F ^b  

^a UNIVERSITY OF GENOA   (Italy)

^b UNIVERSITY OF BOLOGNA   (Italy)

Author keywords

[No Author keywords available]

Indexed keywords

ALUMINA; DEHYDROGENATION; DEPOSITION; PACKED BEDS; PROPANE; PROPYLENE; VANADIUM COMPOUNDS;

CATALYTIC MEMBRANE REACTOR; INTERNAL SURFACE; MONOLITH LIKE REACTOR; OXIDEHYDROGENATION; REACTANTS; TUBULAR POROUS CERAMIC DEVICE; TURNOVER NUMBER; VANADIUM OXIDE;

CATALYSTS;

CATALYSTS; CATALYTIC; CRACKING; HYDROCARBONS; REACTORS; VANADIUM OXIDE;

EID: 0030131426     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/0009-2509(96)00040-1     Document Type: Article

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