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Composite catalyst activity from component coking

Thesis/Dissertation ·
OSTI ID:6124651
Deactivation of a composite acid catalyst during cracking of n-hexadecane was studied using an apparatus consisting of a thermogravimetric analysis (TGA) system operating as a pulse microreactor followed by a gas chromatograph. The composite catalyst, which contains a silica-alumina component and a zeolite component, was compared to the separate, catalytically active, components with respect to activity as a function of coke lay-down. Pretreatment of each component and the composite catalyst was conduced using a helium-heat treatment and a steaming treatment. The untreated zeolite was also tested for comparison of the pretreatment effects. A test was designed and used to compare flow hydrodynamics in different TGAs, used as pulse microreactors. The test involves passing a pulse of injectant over the sample pan containing an adsorbent. The technique is performed in the pulse mode is a similar manner to the deactivation studies and is insensitive to variations in temperature. The test is useful for comparing TGA extent-of-conversion data in this study to similar measurements taken from other reactor configurations, flow rates, and flow geometries. The technique should also prove useful for comparing results of other gas/solid catalytic reactions performed by TGA. A comparison of activity versus surface area and activity versus sample acidity was made. The results of this comparison were found to be consistent with the proposed deactivation model. Several deactivation models were tested and a suitable approach was developed which allows for Partitioned Flow of reactant from the silica-alumina matrix, in the composite catalyst, to the zeolite.
Research Organization:
West Virginia Univ., Morgantown, WV (USA)
OSTI ID:
6124651
Country of Publication:
United States
Language:
English