2014
DOI: 10.1016/b978-0-12-419974-3.00002-6
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Kinetics of Catalytic Dehydrogenation of Propane over Pt-Based Catalysts

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Cited by 22 publications
(28 citation statements)
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“…However, in contrast with the results from MTD calculations, subsequent C–H bond breaking (in the case R = H) is not favored. 38 40 This difference of reactivity is consistent with the significantly higher selectivity and resulting higher coking resistance of Pt 2 Ga compared to Pt.…”
Section: Results and Discussionsupporting
confidence: 64%
“…However, in contrast with the results from MTD calculations, subsequent C–H bond breaking (in the case R = H) is not favored. 38 40 This difference of reactivity is consistent with the significantly higher selectivity and resulting higher coking resistance of Pt 2 Ga compared to Pt.…”
Section: Results and Discussionsupporting
confidence: 64%
“…The activation energy of the catalysts in this work is in the range of 60-120 kJ/mol, which is reasonable compared to the results reported in the literature. 2,47,48 The activation energy for the catalyst without H2S addition is 62 kJ/mol, while the ones for the catalysts with 3 and 9 ppm of H2S addition increase to 71 kJ/mol and 78 kJ/mol, respectively. Since the activation energy would decrease with less coke deposited on Pt surfaces during PDH based on the literatures, 14,49,50 the increase of activation energy in this work could be ascribed to the presence of H2S, and this effect was investigated by DFT calculations in section 3.4.4.…”
Section: Effect Of H 2 S Addition On Activation Energymentioning
confidence: 99%
“…[11][12][13] However, coking and deactivation of this kind of catalyst are still inevitable problems. 14 In industrial practice, the co-feed of hydrogen 7,[15][16][17][18] or steam 19 with propane is used to enhance the performance of platinum-based catalysts. The presence of hydrogen can contribute to higher propene selectivity and lower coking rates.…”
Section: Introductionmentioning
confidence: 99%
“…Steam has been widely used as an energy carrier, a coke remover and a diluent in dehydrogenation processes. 19,22,23 Introducing steam into the feed can strengthen PDH processes by increasing the propane equilibrium conversion and lowering the temperature drop of the adiabatic dehydrogenation reactors. 19 Dong et al 24 found that under the same propane partial pressure, steam can contribute to higher propene yield compared with that in nitrogen atmosphere.…”
Section: Introductionmentioning
confidence: 99%