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Improved Fischer-Tropsch synthesis catalysts for indirect coal liquefaction: Quarterly technical progress report No. 7 for the period 1 April to 30 June 1987

Technical Report ·
OSTI ID:6125326
Three monomeric supported ruthenium catalysts were evaluated for Fischer-Tropsch performance with 1:1 H/sub 2/:CO synthesis gas at 1 atm. This effort completes the FTS evaluation of a series of nine supported multiatomic and atomic ruthenium catalysts prepared via organometallic reactions of tetra- and hexaruthenium hydridocarbonyls and allyl monoruthenium carbonyl complexes with acid sites on three support materials, alumina, sodium Y zeolite, and molecular sieve. The ruthenium catalyst supported on sodium Y zeolite had superior FTS performance relative to a conventionally prepared alumina-supported ruthenium catalyst. Its chain growth factor was higher, methane selectivity lower, and olefin-to-paraffin ratio for light hydrocarbons higher. The results for the molecular sieve catalyst under the same reaction conditions were inferior with low chain growth parameter and high methane selectivity. The C/sub 2+/ hydrocarbon synthesis rates of all the ruthenium catalysts were comparable. The effect of high-level sulfur chemisorption on the FTS performance of alumina-supported cobalt was also examined. The untreated cobalt catalyst had higher activity and higher methane selectivity relative to the standard fused iron catalyst. 4 figs., 2 tabs.
Research Organization:
SRI International, Menlo Park, CA (USA)
DOE Contract Number:
AC22-85PC80016
OSTI ID:
6125326
Report Number(s):
DOE/PC/80016-T5; ON: DE88000883
Country of Publication:
United States
Language:
English