Alan H. Singleton - Baden PA Rachid Oukaci - Gibsonia PA
Assignee:
Energy International Corporation - Pittsburgh PA
International Classification:
B01J 2340
US Classification:
502327, 502415, 502439
Abstract:
A highly active Fischer-Tropsch catalyst having increased thermal stability. The catalyst comprises a -alumina support doped with an amount of lanthana oxide, barium oxide, or a combination thereof effective for increasing the thermal stability of the catalyst in a slurry bubble column reaction system while maintaining or increasing the activity of the catalyst for Fischer-Tropsch synthesis.
Attrition Resistant Fischer-Tropsch Catalyst And Support
Alan H. Singleton - Baden PA Rachid Oukaci - Gibsonia PA James G. Goodwin - Cranberry Township PA
Assignee:
Sasol Technology (UK) Limited - Sasolburg
International Classification:
B01J 2002
US Classification:
502429, 423626, 423628, 502355
Abstract:
A catalyst support having improved attrition resistance and a catalyst produced therefrom. The catalyst support is produced by a method comprising the step of treating calcined -alumina having no catalytic material added thereto with an acidic aqueous solution having an acidity level effective for increasing the attrition resistance of the calcined -alumina.
Attrition Resistant Gamma-Alumina Catalyst Support
Alan H. Singleton - Baden PA, US Rachid Oukaci - Gibsonia PA, US James G. Goodwin - Cranberry Township PA, US
Assignee:
Sasol Technology (UK) Limited - Sasolburg
International Classification:
C01F 7/02 B01J 21/00
US Classification:
423628, 423626, 502355
Abstract:
A γ-alumina catalyst support having improved attrition resistance produced by a method comprising the steps of treating a particulate γ-alumina material with an acidic aqueous solution comprising water and nitric acid and then, prior to adding any catalytic material thereto, calcining the treated γ-alumina.
In Situ Conversion Of Subsurface Hydrocarbon Deposits To Synthesis Gas
Alan H. Singleton - Baden PA, US Richard A. Flinn - Pittsburgh PA, US
International Classification:
E21B 43/24
US Classification:
166369, 166302
Abstract:
A method for producing synthesis gas from underground hydrocarbon deposits is described. Oxygen and water are reacted with the hydrocarbon deposit under conditions conducive to the production of carbon monoxide and hydrogen. The method is applicable to oil reservoirs from which conventional production means are unable to recover additional oil practically, to viscous oil deposits from which production is limited, and to shale oil deposits.
Method Of Forming A Paraffinic Product By Thermal Cracking
Richard A. Flinn - Pittsburgh PA, US Alan H. Singleton - Baden PA, US
International Classification:
C10G 9/00
US Classification:
208106
Abstract:
The present invention relates to a method of forming a paraffinic product that involves providing a paraffinic feed having an initial average carbon chain length of greater than 20. The paraffinic feed is a product of a gas-to-liquids process, such as a Fischer-Tropsch process. The paraffinic feed is subjected to thermal cracking at elevated temperature and elevated pressure, which results in the formation of a paraffinic product. The paraffinic product has a final average carbon chain length of less than or equal to 20. The paraffinic product is typically liquid at ambient temperature, such as at 25 C.
Regeneration Of Alkanolamine Absorbing Solution In Gas Sweetening Processes
Otto A. Homberg - Easton PA Charles W. Sheldrake - Bethlehem PA Alan H. Singleton - Baden PA
Assignee:
Bethlehem Steel Corporation - Bethlehem PA
International Classification:
B01D 5334
US Classification:
423228
Abstract:
A catalytic amount of ammonia or ammonium compounds are utilized to prevent deterioration of alkanolamines employed in gas sweetening processes. The ammonia is added either to the sour gas or the absorbing solution and acts to suppress thiocyanate. [. formation. ]. . Iadd. accumulation. Iaddend. during absorption. BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to gas purification and more particularly to gas purification by the removal of acid gases from industrial gas in an absorption/desorption process. 2. Prior Art The term "gas sweetening" pertains to gas purification processes in which acid gases, particularly sulfurous gases are removed from industrial gases. Gas sweetening processes commonly utilize aqueous absorbing solutions into which the acid gases are scrubbed (absorbed) to be later stripped (desorbed) for possible further treatment. Desorbing is accomplished by heating the spent solution to expel the acid gases.
Reducing Fischer-Tropsch Catalyst Attrition Losses In High Agitation Reaction Systems
Alan H. Singleton - Baden PA Rachid Oukaci - Gibsonia PA James G. Goodwin - Cranberry Township PA
Assignee:
Energy International Corporation - Pittsburgh PA
International Classification:
C07C 2700 B01J 2300 B01J 2340
US Classification:
518715
Abstract:
A method for reducing catalyst attrition losses in hydrocarbon synthesis processes conducted in high agitation reaction systems; a method of producing an attrition-resistant catalyst; a catalyst produced by such method; a method of producing an attrition-resistant catalyst support; and a catalyst support produced by such method. The inventive method of reducing catalyst attrition losses comprises the step of reacting a synthesis gas in a high agitation reaction system in the presence of a catalyst. In one aspect, the catalyst preferably comprises a. gamma. -alumina support including an amount of titanium effective for increasing the attrition resistance of the catalyst. In another aspect, the catalyst preferably comprises a. gamma. -alumina support which has been treated, after calcination, with an acidic, aqueous solution. The acidic aqueous solution preferably has a pH of not more than about 5.
Processes And Palladium-Promoted Catalysts For Conducting Fischer-Tropsch Synthesis