skip to main content
OSTI.GOV title logo U.S. Department of Energy
Office of Scientific and Technical Information

Title: Cobalt-based catalysts for the production of C/sub 2/-C/sub 4/ hydrocarbons from syn(thesis) gas

Journal Article · · ACS Symp. Ser.; (United States)
OSTI ID:6015651

A total of 12 catalysts, including a 100 Co/10 Cu/13 ThO/sub 2//200 kieselguhr reference catalyst, 100 Co/10 Cr/200 kieselguhr, 100 Co/3.7 Zr/200 kieselguhr, and eight Co-Mn catalysts, with 100:5, 100:10, and 100:50 cobalt-manganese ratios, prepared by impregnation of kieselguhr or alumina by metal nitrates, some of which contained various small amounts of K/sub 2/O, were screened in a Berty internally recycled catalytic reactor at 193/sup 0/-370/sup 0/C, 100 psig, and 1:3:6 CO-H/sub 2/-He feed composition. Chromium- and zirconium-doped catalysts were the most active for CO conversion (25 and 18.5%) but also the most selective for methane (n; 99.9%). At low temperatures, e.g., 219/sup 0/C, the yield of C/sub 2/-C/sub 3/ olefins was n; 32% of the gaseous products, but it rapidly decreased to almost zero at higher temperatures (over 238/sup 0/C). The Co-Mn catalysts containing K/sub 2/O showed higher selectivities for olefins (up to 37.6% by wt) but low activities. The 100 Co/50 Mn/400 Al/sub 2/O/sub 3//5.5 K/sub 2/O catalyst seems to be the most promising for an economic coal-based Fischer-Tropsch process. Future studies will include alumina-supported, K/sub 2/O-doped Fe-Co, Fe-Mn, and Fe-Mn-Co. Diagrams, tables, graphs, and 12 references.

Research Organization:
Carnegie-Mellon Univ., Pittsburgh, PA
OSTI ID:
6015651
Journal Information:
ACS Symp. Ser.; (United States), Vol. 23:2
Country of Publication:
United States
Language:
English