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U.S. Department of Energy
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Crystallite size and support effects on CO hydrogenation reactions. Final progress report, January 1, 1982-August 30, 1984

Technical Report ·
OSTI ID:6952284
TiO/sub 2/-supported Pd was found to be the most active Pd methanation catalyst yet reported. However, in-situ IR studies showed that almost no IR-active CO was present on the Pd surface during reaction. During this time, similar results were found for Pt, as Pt/TiO/sub 2/ catalysts were found to be 100 times more active than Pt/SiO/sub 2/ catalysts and 10 times more active than Pt/Al/sub 2/O/sub 3/ and Pt/SiO/sub 2/-Al/sub 2/O/sub 3/ catalysts. Again surface concentrations of IR-active CO were barely detectable under reaction conditions. Both H/sub 2/ and CO chemisorption measurements were conducted on these catalysts. The surface concentrations of CO under reaction conditions indicated that only a small fraction (1-2%) of the TiO/sub 2/-supported metal surface was covered by CO. As a consequence, a modified model for the methanation reaction was proposed, and it was inferred from the studies on Pt and Pd that only a small fraction of the surface metal atoms constitute active sites which create these higher activities.
Research Organization:
Pennsylvania State Univ., University Park (USA). Dept. of Chemical Engineering
DOE Contract Number:
AC02-77ER04463
OSTI ID:
6952284
Report Number(s):
DOE/ER/04463-7; ON: DE84012474
Country of Publication:
United States
Language:
English