Similar effect of carbon and silica catalyst support on the hydrogenation reaction rate in organic slurry reactors

Chemical Engineering Science

Volumn 60, Issue 22, 2005, Pages 6492-6503

  Ruthiya, K C ^a   Van Der Schaaf, J ^a   Kuster, B F M ^a   Schouten, J C ^a  

^a EINDHOVEN UNIVERSITY OF TECHNOLOGY   (Netherlands)

Author keywords

Gas hold up; Hydrogenation; Mass transfer; Modeling; Reaction engineering; Slurry bubble column; Stirred slurry reactor

Indexed keywords

ADHESION; CARBON; CHEMICAL REACTORS; HYDROGENATION; MASS TRANSFER; MATHEMATICAL MODELS; PALLADIUM; REACTION KINETICS; SILICA; SLURRIES;

HYDROGENATION REACTIONS; MASS TRANSPORT; REACTION RATES; SILICA CATALYST;

CATALYST ACTIVITY;

BUBBLE COLUMN; HOLD-UP; HYDROGENATION; MASS TRANSFER; SLURRY;

EID: 22744459337     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2005.03.034     Document Type: Conference Paper

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