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U.S. Department of Energy
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Promoter modifications of catalytic activity and selectivity. Progress report, April 1, 1982-March 31, 1983

Technical Report ·
OSTI ID:6461234
The influence of alkali promoters on CO hydrogenation was studied as a function of catalyst support (Al/sub 2/O/sub 3/, SiO/sub 2/, SiO/sub 2/.Al/sub 2/O/sub 3/ and TiO/sub 2/). Temperature-programmed reaction was used to study the specific rates of CO and carbon hydrogenation, and temperature-programmed desorption studied the change in H/sub 2/ and CO desorption rates. The role of the support was separately studied for comparison. Specific-activity and product distributions were also studied in a differential reactor with gas-chromatography detection. On all catalysts the selectivity for higher hydrocarbons, particularly olefins, was increased by addition of Na or K promoters. On all catalysts but Ni/SiO/sub 2/.Al/sub 2/O/sub 3/, however, the specific activity decreased; on Ni/SiO/sub 2/.Al/sub 2/O/sub 3/, a slight increase in specific activity was seen. Similarly, significant changes in methanation activation energies were observed for the addition of promoters. Good agreement was obtained between differential reactor studies and temperature-programmed reaction. The role of the promotor is significantly influenced by the oxide support. 12 figures, 4 tables.
Research Organization:
Colorado Univ., Boulder (USA). Dept. of Chemical Engineering
DOE Contract Number:
AC02-82ER12058
OSTI ID:
6461234
Report Number(s):
DOE/ER/12058-1; ON: DE83010916
Country of Publication:
United States
Language:
English

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