2017
DOI: 10.1039/c6cy02329k
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The effect of water on methane oxidation over Pd/Al2O3 under lean, stoichiometric and rich conditions

Abstract: Methane conversion during cooling ramp: water inhibits methane conversion more severely in high oxygen concentration.

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Cited by 51 publications
(35 citation statements)
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“…The temperature delay is 100°C, which correlates well with the methane combustion reactivity tests on palladium catalysts 24,60 . Typically, when water is added to the reaction mixture, a positive shift (35-120°C temperature range) of T 50 (temperature at which 50% methane conversion is achieved) is measured 25,68 . The turnover rate for methane oxidation was found to decrease by 95% when PdO decomposed to Pd metal at 888 K, showing that PdO is more active than Pd metal for methane combustion at this temperature 69 .…”
Section: Discussionmentioning
confidence: 99%
“…The temperature delay is 100°C, which correlates well with the methane combustion reactivity tests on palladium catalysts 24,60 . Typically, when water is added to the reaction mixture, a positive shift (35-120°C temperature range) of T 50 (temperature at which 50% methane conversion is achieved) is measured 25,68 . The turnover rate for methane oxidation was found to decrease by 95% when PdO decomposed to Pd metal at 888 K, showing that PdO is more active than Pd metal for methane combustion at this temperature 69 .…”
Section: Discussionmentioning
confidence: 99%
“…[15][16][17] The methane oxidation over palladium-alumina formulations is known to be inhibited by water present in the combustion exhaust and/or generated by the complete methane oxidation reaction itself. [18][19][20][21] Previous studies report that the inhibition is caused by formation of hydroxyl groups and/or adsorbed water blocking the catalytically active PdO sites. [22][23][24][25][26][27][28][29][30][31] Also the formation of an inactive PdIJOH) 2 phase and site blocking by carbonates have been brought forward as additional deactivation mechanisms.…”
Section: Introductionmentioning
confidence: 99%
“…[18][19][20][21] Previous studies report that the inhibition is caused by formation of hydroxyl groups and/or adsorbed water blocking the catalytically active PdO sites. [22][23][24][25][26][27][28][29][30][31] Also the formation of an inactive PdIJOH) 2 phase and site blocking by carbonates have been brought forward as additional deactivation mechanisms. [32][33][34] In the case of water inhibition, infrared spectroscopic measurements evidence that hydroxyl groups build up on the alumina surface both by spill-over of reaction products and direct water dissociation.…”
Section: Introductionmentioning
confidence: 99%
“…It has therefore found great applications in modern industry, such as catalytic exhaust converters aimed to reduce methane emission and catalytic gas turbine combustors designed to combust fuel under mild conditions [9,10]. Supported PdO catalysts have shown excellent catalytic property in methane oxidation, and currently are under extensive study [11][12][13][14][15][16][17][18]. However, once sulfur species (e.g., H 2 S or SO 2 ) are present in the reaction atmosphere, the poisoning of PdO catalyst which would lead to inactive PdO-SO x is irreversible and the activity of the catalyst cannot be recovered at relatively low temperature [19][20][21][22][23][24][25].…”
Section: Introductionmentioning
confidence: 99%