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Reaction Kinetics of an Industrial Front‐End Acetylene Hydrogenation Catalyst Using the Advanced TEMKIN Reactor
The front‐end process integration of the selective acetylene hydrogenation provides several advantages over the tail‐end option. But extensive knowledge of the process and reaction kinetics are required. This work combines the ideal conditions of the advanced TEMKIN reactor in a laboratory plant for gradient‐free kinetic analysis of eggshell catalyst under industrially relevant front‐end conditions. With this system an industrial state of the art Pd‐Ag/Al2O3 eggshell catalyst is investigated and the temperature dependent data under various feed compositions including information on the formation of C4‐species are reported.
Reaction Kinetics of an Industrial Front‐End Acetylene Hydrogenation Catalyst Using the Advanced TEMKIN Reactor
The front‐end process integration of the selective acetylene hydrogenation provides several advantages over the tail‐end option. But extensive knowledge of the process and reaction kinetics are required. This work combines the ideal conditions of the advanced TEMKIN reactor in a laboratory plant for gradient‐free kinetic analysis of eggshell catalyst under industrially relevant front‐end conditions. With this system an industrial state of the art Pd‐Ag/Al2O3 eggshell catalyst is investigated and the temperature dependent data under various feed compositions including information on the formation of C4‐species are reported.
Reaction Kinetics of an Industrial Front‐End Acetylene Hydrogenation Catalyst Using the Advanced TEMKIN Reactor
Hock, Sebastian (Autor:in) / Iser, Leonhard (Autor:in) / Lucas, Martin (Autor:in) / Rose, Marcus (Autor:in)
Chemie Ingenieur Technik ; 94 ; 1704-1710
01.11.2022
7 pages
Aufsatz (Zeitschrift)
Elektronische Ressource
Englisch
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