TY - GEN
T1 - Fischer-Tropsch synthesis
T2 - 11th Topical Conference on Gas Utilization 2011 - Topical Conference at the 2011 AIChE Spring Meeting and 7th Global Congress on Process Safety
AU - Gnanamani, Muthu Kumaran
AU - Ribeiro, Mauro C.
AU - Ma, Weinping
AU - Jacobs, Gary
AU - Graham, Uschi M.
AU - Shafer, Wilson D.
AU - Davis, Burtron H.
PY - 2011
Y1 - 2011
N2 - The reaction of carbon monoxide and hydrogen to form hydrocarbons using either an iron or cobalt catalyst usually produces a broad range of products which consists of mainly paraffins and olefins with a carbon number of up to and greater than 100, and low levels of oxygenates including alcohols, aldehydes, ketones and acids. Iron catalysts usually produce more olefins and oxygenates compared to supported cobalt catalysts at elevated temperatures and pressures [1,2]. For Fischer-tropsch (FT) synthesis, cobalt has been reported to produce mainly n-alkanes over a wide range of molecular weights. The cobalt active phase is generally deposited over an oxide support (e.g., Al2O3, SiO2, or TiO2), which provides good mechanical strength (i.e., attrition resistance) and thermal stability under reaction conditions. Factors such as particle size and shape, metal loading and dispersion, nature of the support and strength of metal-support interactions have been widely studied over supported cobalt-based catalysts [3,4]. Many interesting studies have been devoted to ascertain the influence of oxide support on the FT activity, selectivity, and stability of cobalt catalysts.
AB - The reaction of carbon monoxide and hydrogen to form hydrocarbons using either an iron or cobalt catalyst usually produces a broad range of products which consists of mainly paraffins and olefins with a carbon number of up to and greater than 100, and low levels of oxygenates including alcohols, aldehydes, ketones and acids. Iron catalysts usually produce more olefins and oxygenates compared to supported cobalt catalysts at elevated temperatures and pressures [1,2]. For Fischer-tropsch (FT) synthesis, cobalt has been reported to produce mainly n-alkanes over a wide range of molecular weights. The cobalt active phase is generally deposited over an oxide support (e.g., Al2O3, SiO2, or TiO2), which provides good mechanical strength (i.e., attrition resistance) and thermal stability under reaction conditions. Factors such as particle size and shape, metal loading and dispersion, nature of the support and strength of metal-support interactions have been widely studied over supported cobalt-based catalysts [3,4]. Many interesting studies have been devoted to ascertain the influence of oxide support on the FT activity, selectivity, and stability of cobalt catalysts.
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M3 - Conference contribution
AN - SCOPUS:84907074986
SN - 9781617828942
T3 - 11th Topical Conference on Gas Utilization 2011 - Topical Conference at the 2011 AIChE Spring Meeting and 7th Global Congress on Process Safety
SP - 297
EP - 298
BT - 11th Topical Conference on Gas Utilization 2011 - Topical Conference at the 2011 AIChE Spring Meeting and 7th Global Congress on Process Safety
Y2 - 13 March 2011 through 17 March 2011
ER -