Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Study of Fischer-Tropsch synthesis over iron-based catalysts using a well-stirred slurry reactor

Thesis/Dissertation ·
OSTI ID:6174982
Fischer-Tropsch synthesis over iron catalysts has been researched for well over 60 years, yet relatively few detailed investigations of the kinetics and selectivity of hydrocarbon synthesis have been done using unpromoted bulk iron-based catalysts. In this investigation, Fe/sub 2/O/sub 3/, potassium-promoted Fe/sub 2/O/sub 3/, fused iron, Fe/sub 3/C, and Fe were tested for their activity and selectivity for hydrocarbon synthesis, and comparisons were made between the catalysts. Experiments were done using a well-stirred slurry reaction which was free of temperature and concentration gradients. The effluent from the reactor was analyzed on line using a dual-column gas chromatograph. The compositions of fresh and used catalyst samples were determined using X-ray diffraction. The activity of fused iron catalyst increases with extent of reduction in H/sub 2/ - attributed to increases in surface area. Principal products are normal 1-olefins and paraffins, CO/sub 2/, H/sub 2/O; branched olefins, aldehydes and alcohols are also formed. The catalyst has very little hydrogenation or isomerization activity due to potassium promotion. Aldehydes reduce to alcohols; the water-gas-shift reaction occurs. The kinetics and selectivity observed using potassium-promoted Fe/sub 2/O/sub 3/ were nearly identical to those of fused iron. In the absence of promoter, the products are almost exclusively n-olefins, n-paraffins, CH/sub 3/OH, H/sub 2/O, CO/sub 2/. Fe/sub 2/O/sub 3/ is active for hydrogenation and isomerization.
Research Organization:
California Univ., Berkeley (USA)
OSTI ID:
6174982
Country of Publication:
United States
Language:
English