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

Improved catalysts for coal liquefaction. Quarterly report No. 3, March 1-May 31, 1985

Technical Report ·
OSTI ID:5664379
Shakedown runs of the bench scale hydrotreating unit were initiated in May. The only serious operational problem experienced was an adherence of viscous product to the walls of the high pressure accumulator. This made it difficult to close a material balance around the unit. New product accumulators have been designed which can be removed from the unit and weighed for liquid product yield. The temperature programmed desorption apparatus is proving to be a valuable tool for characterizing surface acidity. An AMOCO exploratory silica-alumina support exhibits a well-defined ..beta..-peak indicating a substantial number of acid sites. The ..beta..-peak was essentially absent in a silica support, and an alumina support was characterized by a wide poorly resolved ..beta..-peak which suggests a wide distribution of acid site strengths. The high acidities reported previously for the hydrotreating catalysts are due to metals loading, and in particular loading with molybdenum. Indications are that the metal sulfides may be less acidic than the oxides. An alumina-aluminum phosphate composite has been prepared in which practically all the pore volume is in pores larger than 5 ..mu..m. The coal derived feedstock has been subjected to further analysis by proton and carbon-13 NMR. 7 refs., 10 figs., 4 tabs.
Research Organization:
Wyoming Univ., Laramie (USA). Dept. of Chemical Engineering
DOE Contract Number:
FG22-84PC70812
OSTI ID:
5664379
Report Number(s):
DOE/PC/70812-3; ON: DE85014156
Country of Publication:
United States
Language:
English