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U.S. Department of Energy
Office of Scientific and Technical Information

New and improved dispersion and recovery techniques for slurry phase catalysis. Quarterly report, October-December 1984

Technical Report ·
OSTI ID:5900450
The present report concerns an investigation of the influence of catalyst pellet particle size on the hydrogenation of naphthalene. The objective of this phase of the work was to investigate, in both a theoretical and experimental manner, the effect of catalyst particle size on the selectivity for tetralin production, i.e. the amount of tetralin produced at a given naphthalene conversion. The hydrogenation of naphthalene was studied experimentally in batch microreactors in the presence of a NiMo/Al/sub 2/O/sub 3/ supported catalyst. Five catalyst particle sizes were utilized in the experimental program: 1/10'', 1/16'', 1/32'', and 1/64'' pellets, and powdered catalyst (-80 US mesh or smaller). Naphthalene was hydrogenated to form tetralin, which was further hydrogenated to form decalins. This system was mathematically modeled as first order consecutive catalytic reactions. A mathematical analysis was developed to predict the behavior of such a reaction system. Experimental results were in fair agreement with theoretical predictions. Naphthalene conversion increased with decreasing catalyst to produce tetralin (an active H-donor in coal liquefaction processes) increased with a decrease in catalyst particle size, in agreement with theoretical predictions. 20 refs., 29 figs., 13 tabs.
Research Organization:
Auburn Univ., AL (USA). Coal Conversion Lab.
DOE Contract Number:
AC22-83PC60044
OSTI ID:
5900450
Report Number(s):
DOE/PC/60044-T5; ON: DE85011811
Country of Publication:
United States
Language:
English