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

Improved catalysts for coal liquefaction. Quarterly report No. 5, September 1, 1985-November 30, 1985

Technical Report ·
OSTI ID:6378332
Three bench scale hydrotreating runs were completed during the last quarter using a distillate fraction of a coal pyrolysis oil as the feedstock. The first of these, Run BMC05, was a process variable study which was terminated after nearly 400 hours of continuous operation. A kinetics model for specific gravity reduction was developed from these data. The decelopment of kinetics models for hydrogen uptake and heteroatom removal must await completion of the analytical workup of the liquid products. Two deactivation runs were undertaken to explore the effects of sodium impregnation on catalyst deactivation rate. Analytical workup of the products is not yet complete. A number od exploratory catalyst preparations were characterized by temperature programmed desorption (TPD) of an organic base. The acidity of a WO/sub 3//alumina catalyst was similar to MoO/sub 3//alumina. The acidity of sulfided molybdate on a carbon support was almost nil. This is surprising the view of our results with alumina based catalysts and the fact that unsupported MoS/sub 2/ prepared by thermal decomposition of ammonium thiomolybdate is acidic. Hydrotreating catalysts containing various additives - magnesium, phosphorous, cobalt and nickel have also been characterized. 14 refs., 7 figs., 4 tabs.
Research Organization:
Wyoming Univ., Laramie (USA). Dept. of Chemical Engineering
DOE Contract Number:
FG22-84PC70812
OSTI ID:
6378332
Report Number(s):
DOE/PC/70812-5; ON: DE86004551
Country of Publication:
United States
Language:
English