Kinetics and reactor modeling of a Pd-Ag/Al2O3 catalyst during selective hydrogenation of ethyne

Applied Catalysis A: General

Volumn 445-446, Issue , 2012, Pages 107-120

  Pachulski, Axel ^a,b   Schödel, Rainer ^a   Claus, Peter ^b  

^a CRI Catalyst Leuna GmbH   (Germany)

^b DARMSTADT UNIVERSITY OF TECHNOLOGY   (Germany)

Author keywords

Alumina; Ethane; Ethene; Ethyne hydrogenation; Kinetic; Mass and heat transfer; Palladium; Silver; Thermodynamic consistency

Indexed keywords

ACTIVE SITE; BEST FIT; BYPASS REACTOR; DETAILED KINETICS; ETHENE; ETHYNE HYDROGENATION; FIXED BED REACTOR; HYDROGENATION REACTORS; KINETIC MEASUREMENT; KINETIC MODELS; LANGMUIR-HINSHELWOOD; POWER LAW EQUATION; PROCESS CONDITION; REACTION MECHANISM; REACTOR MODELING; REACTOR MODELS; RUNNING-IN; SELECTIVE HYDROGENATION; STEAM CRACKER; THERMODYNAMIC CONSISTENCY;

ACETYLENE; ALUMINA; CATALYSTS; CHEMICAL REACTORS; ETHANE; ETHYLENE; HEAT TRANSFER; HYDROGENATION; KINETIC THEORY; PALLADIUM; SILVER; STEAM CRACKING;

KINETICS;

EID: 84870354757     PISSN: 0926860X     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.apcata.2012.08.018     Document Type: Article

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