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Promoter modifications of catalytic activity and selectivity. Progress report, April 1, 1982-November 30, 1983

Technical Report ·
OSTI ID:5659377
Carbon monoxide hydrogenation to methane and higher hydrocarbons was changed significantly by the addition of alkali promoters to supported nickel catalysts. Alkali promoters in general were observed to decrease activity and increase olefin selectivity. However, the oxide support significantly affects the modifications induced by the promoters. On SiO/sub 2/, Al/sub 2/O/sub 3/ and TiO/sub 2/, overall activity decreased; on SiO/sub 2/.Al/sub 2/O/sub 3/, activity increased with promoters and a maximum was observed at low potassium concentrations. Differential reactor studies were also used to show that the support and promoter concentrations had a larger influence on activity and selectivity than catalyst preparation (pre-, co- or postimpregnation) and promoter salt used (KCl, K/sub 2/CO/sub 3/, K/sub 2/C/sub 2/O/sub 4/, KOH). Temperature-programmed reaction (TPR) also showed that alkali decreased the rates of both carbon monoxide and carbon hydrogen; the decreased rates were not due to site blocking. Excellent agreement was obtained between TPR and steady-state kinetics. Temperature-programmed desorption indicated that the decreased hydrogenation rates of CO, carbon and of olefin were due to weakened hydrogen bonding. The CO desorption was also significantly changed by promotion.
Research Organization:
Colorado Univ., Boulder (USA). Dept. of Chemical Engineering
DOE Contract Number:
AC02-82ER12058
OSTI ID:
5659377
Report Number(s):
DOE/ER/12058-2; ON: DE84003179
Country of Publication:
United States
Language:
English