Fischer--Tropsch study of supported ruthenium catalysts
Journal Article
·
· J. Catal.; (United States)
The effect of catalyst support on the activity and product selectivity of CO hydrogenation by ruthenium is discussed. The specific activity of supported ruthenium is dependent upon the nature of the support and on the metal loading. The specific activity for both CO conversion and CH/sub 4/ production increases with increasing metal particle size, obtained either by increasing the metal loading on a given support or by choosing a support which poorly disperses the metal. Supported catalysts with large particles are similar to unsupported ruthenium in activity, but not in selectivity. Product selectivity is characterized by olefin/saturate ratio, length of the hydrocarbon chain, and tendency to produce branched-chain hydrocarbons. Selectivity is a function of both the support and the metal loading. The degree of saturation in the products increases with increasing CO conversion. The length of the hydrocarbon chain is dependent upon temperature, pressure, and nature of the support, but not on the degree of CO conversion. Branched-chain hydrocarbons are produced utilizing acidic supports such as silica-alumina or zeolites, by subsequent isomerization of the initially formed straight-chain products. It is suggested that the support may alter the catalytic behavior of ruthenium through both electronic and dispersional effects. 4 figures, 5 tables.
- Research Organization:
- Amoco Oil Co., Naperville, IL
- OSTI ID:
- 5192485
- Journal Information:
- J. Catal.; (United States), Journal Name: J. Catal.; (United States) Vol. 51:3; ISSN JCTLA
- Country of Publication:
- United States
- Language:
- English
Similar Records
Structure-activity relationships of ruthenium Fischer-Tropsch catalysts (metal particle size effects)
Effect of preparation methods on the catalytic properties of zeolite-supported ruthenium in the Fischer-Tropsch synthesis
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Thesis/Dissertation
·
Sat Dec 31 23:00:00 EST 1988
·
OSTI ID:6438481
Effect of preparation methods on the catalytic properties of zeolite-supported ruthenium in the Fischer-Tropsch synthesis
Journal Article
·
Sat Oct 01 00:00:00 EDT 1983
· J. Catal.; (United States)
·
OSTI ID:5597125
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Thesis/Dissertation
·
Fri Dec 31 23:00:00 EST 1982
·
OSTI ID:6347048
Related Subjects
01 COAL, LIGNITE, AND PEAT
010404 -- Coal
Lignite
& Peat-- Gasification
090121* -- Hydrocarbon Fuels-- Chemical Synthesis-- (1976-1989)
10 SYNTHETIC FUELS
37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400201 -- Chemical & Physicochemical Properties
ALKANES
CARBON COMPOUNDS
CARBON MONOXIDE
CARBON OXIDES
CATALYSTS
CATALYTIC EFFECTS
CHALCOGENIDES
CHEMICAL REACTIONS
CRYOGENIC FLUIDS
ELEMENTS
FISCHER-TROPSCH SYNTHESIS
FLUIDS
HYDROCARBONS
ISOMERIZATION
METALS
METHANATION
METHANE
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
PLATINUM METALS
PRESSURE DEPENDENCE
REFRACTORY METALS
RUTHENIUM
SYNTHESIS
TEMPERATURE DEPENDENCE
TRANSITION ELEMENTS
010404 -- Coal
Lignite
& Peat-- Gasification
090121* -- Hydrocarbon Fuels-- Chemical Synthesis-- (1976-1989)
10 SYNTHETIC FUELS
37 INORGANIC, ORGANIC, PHYSICAL, AND ANALYTICAL CHEMISTRY
400201 -- Chemical & Physicochemical Properties
ALKANES
CARBON COMPOUNDS
CARBON MONOXIDE
CARBON OXIDES
CATALYSTS
CATALYTIC EFFECTS
CHALCOGENIDES
CHEMICAL REACTIONS
CRYOGENIC FLUIDS
ELEMENTS
FISCHER-TROPSCH SYNTHESIS
FLUIDS
HYDROCARBONS
ISOMERIZATION
METALS
METHANATION
METHANE
ORGANIC COMPOUNDS
OXIDES
OXYGEN COMPOUNDS
PLATINUM METALS
PRESSURE DEPENDENCE
REFRACTORY METALS
RUTHENIUM
SYNTHESIS
TEMPERATURE DEPENDENCE
TRANSITION ELEMENTS