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U.S. Department of Energy
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Investigation of sulfur-tolerant catalysts for selective synthesis of hydrocarbon liquids from coal-derived gases. Quarterly technical progress report, March 19-June 18, 1982

Technical Report ·
OSTI ID:6743094
More active supported boride-promoted catalysts were prepared by heating less rapidly during reduction. Unsupported iron and 15% iron on silicalite catalysts were also prepared. Thermogravimetric analysis of prepared samples was also begun. Two silica supported catalysts derived from Fe(CO)/sub 5/ were tested. Both catalysts lost over half their initial activity within five hours, but both steady state activity and product selectivities are comparable with other iron catalysts. A silica-supported, boron-promoted cobalt catalyst was tested and exhibited a selectivity of 72% to C/sub 5/-C/sub 15/ hydrocarbons at temperatures above 485/sup 0/K. Data analysis was completed on in-situ poisoning tests. Exposure to 2 ppM H/sub 2/S resulted in much more rapid deactivation than exposure to 4 to 8 ppM H/sub 2/S. Deactivation at 525/sup 0/K caused an increase in the C/sub 2/ olefin/paraffin ratio.
Research Organization:
Brigham Young Univ., Provo, UT (USA)
DOE Contract Number:
AC22-79ET14809
OSTI ID:
6743094
Report Number(s):
DOE/ET/14809-11; ON: DE83000310
Country of Publication:
United States
Language:
English