Joseph G. Duff - League City TX, US Cecil G. McFarland - League City TX, US
International Classification:
B01D 53/72 B01D 53/96
US Classification:
4232451
Abstract:
The present discloses a process and catalyst therefor to selectively remove acetylenes from gaseous streams in the vapor phase. The process is particularly suitable for high yield recovery of olefinic hydrocarbons from gaseous streams in refinery processes.
A catalyst for removing acetylenic impurities from gaseous organic product streams, comprising at least Fe and Ni, other elements from Groups 8, 1b, 2b, 4b, 6b and 7b of the Periodic Table, an alkaline earth metal and an alkali metal.
A catalyst for removing acetylenic impurities from gaseous organic product streams, comprising at least Fe and Ni, other elements from Groups 8, 1b, 2b, 4b, 6b and 7b of the Periodic Table, an alkaline earth metal and an alkali metal.
A catalyst for removing acetylenic impurities from gaseous organic product streams, comprising at least Fe and Ni, other elements from Groups 8, 1b, 2b, 4b, 6b and 7b of the Periodic Table, an alkaline earth metal and an alkali metal.
Process For Selective Removal Of Acetylenes From Gaseous Streams
- Houston TX, US Cecil G. McFarland - League City TX, US
International Classification:
C07C 7/148 B01J 23/94 B01J 23/78
Abstract:
The present discloses a process and catalyst therefor to selectively remove acetylenes from gaseous streams in the vapor phase. The process is particularly suitable for high yield recovery of olefinic hydrocarbons from gaseous streams in refinery processes.
Controllability Oxidative Dehydrogenation Process For Producing Butadiene
- Houston TX, US Joseph G. Duff - League City TX, US Sirisha Chada - Houston TX, US Elizabeth Ballard - Houston TX, US Cecil G. McFarland - League City TX, US
International Classification:
C07C 5/48 C07C 5/09
US Classification:
585254, 585501
Abstract:
Butadiene is made from a butene rich feed, passing a superheated butene rich feed including superheated steam and oxygen at a temperature of at least about 343 C. (650 F.) over a catalyst bed having a depth of over about 69 cm (27 inches) of granules of ferritic oxidative dehydrogenation catalyst. Inlet conditions being controlled such that the oxidative dehydrogenation reactions initially occur in the lower most layers of catalyst. Process control includes monitoring the temperature throughout the bed and increasing the inlet temperature in response to a drop in the temperature in the active layer, when the active layer of oxidative dehydrogenation catalyst begins to become deactivated so that the reaction zone moves upwardly in the oxidative dehydrogenation bed.
Cecil McFarland 1977 graduate of David Douglas High School in Portland, OR is on Classmates.com. See pictures, plan your class reunion and get caught up with Cecil and other high school alumni