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

Novel approaches concerning catalyst deactivation. Final report, May 1, 1981-April 31, 1982

Technical Report ·
OSTI ID:6231932
Catalyst deactivation is a problem of particular severity for the processes of catalytic coal liquefaction and hydrotreatment of coal-derived liquids. The cost of catalyst replacement, resulting from catalyst deactivation, could conservatively be placed in the range of $2 to $3 per bbl of oil recovered and this is not necessarily the real problem, since the availability of catalytically active metals such as Co, Mo and Ni is a more severe problem than their cost. The experimental findings in this area have been summarized in a series of recent publications and reports. In our recent publication an effort was made to explain the existence of an optimum catalyst size by use of simplified shell-type deactivation models. In this paper we study in detail a mathematical model which has been used with considerable success in modelling the experimental behavior of catalytic coal hydroliquefaction and coal liquid hydrotreatment processes. The purpose of this study is to investigate theoretically the existence and develop, when possible, simple algebraic expressions which predict a catalyst size, average pore size and pore size distribution which yield the best overall catalyst performance and activity. The motivation for this work was our desire to understand, at least qualitatively, the intricate experimental behavior of the catalytic coal hydroliquefaction reaction system. However, the results could conceivably apply to other industrial processes described by lumped kinetic models for which deactivation occurs by smiultaneous site coverage and pore blockage.
Research Organization:
University of Southern California, Los Angeles (USA). Dept. of Chemical Engineering
DOE Contract Number:
FG22-81PC41263
OSTI ID:
6231932
Report Number(s):
DOE/PC/41263-T1; ON: DE83010890
Country of Publication:
United States
Language:
English