2018
DOI: 10.1007/s11237-018-9536-z
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Catalytic Activity and Resistance to Sulfur Poisoning of Nickel-Containing Composites Based on Stabilized Zirconia in Tri-reforming of Methane

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Cited by 12 publications
(9 citation statements)
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“…In methane reforming processes, catalyst poisoning due to the strong chemisorption of impurities on active sites of catalyst is unpreventable as the methane source (i.e., biogas and natural gas) typically contains a minor amount of H 2 S [79]. According to literature [50,80], the adsorption of H 2 S molecules on metal surface would lead to surface coverage and subsequently dissociates through the formation of a bulk sulfide phase. The formation of sulfur-containing compounds on the metal surface inhibits the accessibility of reactants to the active sites of metal particles and thus, suppression on the surface reaction.…”
Section: Catalyst Poisoningmentioning
confidence: 99%
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“…In methane reforming processes, catalyst poisoning due to the strong chemisorption of impurities on active sites of catalyst is unpreventable as the methane source (i.e., biogas and natural gas) typically contains a minor amount of H 2 S [79]. According to literature [50,80], the adsorption of H 2 S molecules on metal surface would lead to surface coverage and subsequently dissociates through the formation of a bulk sulfide phase. The formation of sulfur-containing compounds on the metal surface inhibits the accessibility of reactants to the active sites of metal particles and thus, suppression on the surface reaction.…”
Section: Catalyst Poisoningmentioning
confidence: 99%
“…Kantserova et al [80] scrutinised the catalytic activity of Ni-containing composites (i.e., Ni-Cu-CeO 2 , Pd-Ni, and Pt-Ni) and their resistance to sulfur poisoning for TRM (reaction conditions: 800 • C, 1 bar, molar ratio of CH 4 :CO 2 :H 2 O:O 2 :Ar = 4:6:5:0.5:84.5, inlet gas flowrate =90 mL min − 1 , 3500 ppm H 2 S). The Ni-Cu-CeO 2 catalyst performed a low resistance to sulfur poisoning as it was promptly lost up to 42 % of CH 4 conversion after 70 min of reaction run.…”
Section: Catalyst Poisoningmentioning
confidence: 99%
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“…Small amounts (0.1%) of palladium or platinum added to nickel catalysts for the reforming of methane demonstrated the greatest resistance to the action of H 2 S (3500 ppm). The resistance of the catalysts to the poisoning by H 2 S increases in a sequence that coincides with an order of the corrosion resistance of metal active components of composites in the air saturated with water vapor, containing a trace of hydrogen sulfide (Ni < Pt < Pd) [129].…”
Section: Noble Metalsmentioning
confidence: 80%
“…Many previous studies attempted to address the challenge of catalyst deactivation due to sulfur poisoning [7,8,9,10,11,12]. Sato and Fujimoto studied tar gasification by catalytic steam reforming on a Ni/MgO-CaO catalyst doped with WO3.…”
Section: Introductionmentioning
confidence: 99%