Kinetics and mass transfer in hydroformylation-bulk or film reaction?

Canadian Journal of Chemical Engineering

Volumn 88, Issue 4, 2010, Pages 618-624

  Bernas, Andreas ^a   Wärnå, Johan ^a   Mäki Arvela, Päivi ^a   Murzin, Dmitry Yu ^a   Salmi, Tapio ^a  

^a LABORATORY OF INDUSTRIAL CHEMISTRY AND REACTION ENGINEERING   (Finland)

Author keywords

Gas liquid reaction; Hydroformylation; Kinetics and mass transfer

Indexed keywords

COMPLEX KINETICS; CYCLOHEXYL; DIPHENYLPHOSPHINE; EXPERIMENTAL DATA; GAS-LIQUID REACTION; HOMOGENEOUS CATALYST; HYDROFORMYLATION PROCESS; ISOBUTYRALDEHYDE; KINETIC REGIME; LABORATORY SCALE; LIQUID-PHASE DIFFUSION; LIQUID-PHASE MASS TRANSFER; MODEL SIMULATION; N-BUTYRALDEHYDE; REACTOR MODELS; RHODIUM CATALYSTS; SEMIBATCH REACTOR; STIRRING RATES; SYN-GAS; TRIMETHYL;

BATCH REACTORS; CATALYSTS; COMPUTER SIMULATION; HYDROFORMYLATION; HYDROXYLATION; MASS TRANSFER; PROPYLENE; REACTION RATES; RHODIUM;

LIQUIDS;

EID: 77954712595     PISSN: 00084034     EISSN: 1939019X     Source Type: Journal    
DOI: 10.1002/cjce.20330     Document Type: Article

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