1950
DOI: 10.1021/ie50482a025
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Catalytic Dehydrogenation of Butenes

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Cited by 15 publications
(6 citation statements)
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“…For this catalyst, propane conversions to propylene at 550"C were found to be equilibrium limited (25-30Y0 conversion), with a selectivity of 83-90'XO, illustratingthe effectiveness of this dehydrogenation catalyst. Theoretical calculations based on thermodynamic data indicate an equilibrium conversion of 30% at a temperatureof 540"C for propane dehydrogenation to propylene [86,94].…”
Section: -mentioning
confidence: 99%
“…For this catalyst, propane conversions to propylene at 550"C were found to be equilibrium limited (25-30Y0 conversion), with a selectivity of 83-90'XO, illustratingthe effectiveness of this dehydrogenation catalyst. Theoretical calculations based on thermodynamic data indicate an equilibrium conversion of 30% at a temperatureof 540"C for propane dehydrogenation to propylene [86,94].…”
Section: -mentioning
confidence: 99%
“…Catalyst 1707 of the STANDARD OIL DEVELOPMENT CO. [115], the constituents of which are given in Table 481 and Catalyst 105 of the SHELL DEVELOPMENT CO., the composition of which is given in Table 482, may be mentioned [116]. A catalyst developed by the Dow CHEMICAL CO. also for the dehydrogenation of butane consisted of calcium, nickel, and phosphoric acid in a ratio corresponding to Ca 8 Ni(P0 4 ) e with a content of about 2% of Cr 2 0 3 [117].…”
Section: The Dehydrogenation Ovenmentioning
confidence: 99%
“…The catalytic dehydrogenation of butenes was reported by Kearby (41), who describes modifications in composition of the 1707 catalyst. The main feature of this particular catalyst, which consists of 72.4% magnesia, 18.4% ferric oxide, 4.6% copper oxide, and 4.6% potassium oxide is the high selectivity and stability for the conversion of butenes to butadiene.…”
Section: Reforming and Dehydrogenation Chemical Conceptsmentioning
confidence: 99%