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Citation
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HERO ID
3226339
Reference Type
Journal Article
Title
A comparison of H2S, SO2, and COS poisoning on Ni/YSZ and Ni/K2O-CaAl2O4 during methane steam and dry reforming
Author(s)
Jablonski, WS; Villano, SM; Dean, AM
Year
2015
Is Peer Reviewed?
1
Journal
Applied Catalysis A: General
ISSN:
0926-860X
EISSN:
1873-3875
Publisher
Elsevier
Volume
502
Issue
Elsevier
Page Numbers
399-409
DOI
10.1016/j.apcata.2015.06.009
Web of Science Id
WOS:000361162200046
URL
https://linkinghub.elsevier.com/retrieve/pii/S0926860X15300259
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Abstract
A systematic comparison of sulfur poisoning on Ni/YSZ and Ni/K2O-CaAl2O4, a commercially available reforming catalyst, demonstrated the heightened and rapid degradation of Ni/YSZ methane reforming activity. Ni/K2O-CaAl2O4 has nearly 15 times the hydrogen uptake capacity of Ni/YSZ which implies a difference in active nickel area. Because of this difference in active nickel surface area, Ni/K2O-CaAl2O4 was diluted in pure alpha-Al2O3 to achieve the same active nickel surface area as Ni/YSZ. The turnover frequencies (TOF) for steam methane reforming without sulfur on Ni/YSZ and Ni/K2O-CaAl2O4 were similar, although there was some deactivation on Ni/K2O-CaAl2O4 possibly as a result of coking which was observed visually. Sulfur deactivation on both catalysts was examined for H2S, SO2, and COS at concentrations of 1, 3, and 5 ppm. Ni/YSZ deactivated rapidly to an activity close to zero. Ni/K2O-CaAl2O4 deactivated quickly in the first 20 min, but then reached a non-zero steady state activity. The relative deactivation rates for the sulfur species examined were COS > SO2 >= H2S. Reaction temperatures of 650 degrees C, 750 degrees C, and 800 degrees C were evaluated, but temperature did not strongly affect deactivation rates for either catalyst. The overarching result of this study is that Ni/YSZ methane reforming activity is more sensitive to sulfur deactivation than a commercial reforming catalyst. The effect is so strong, that the use of Ni/YSZ with any hydrocarbon fuel may require removal of sulfur to sub-ppm levels. (C) 2015 Elsevier B.V. All rights reserved.
Keywords
Methane steam reforming; Methane dry reforming; CO2 reforming; Hydrogen sulfide; Sulfur dioxide; Ni/YSZ; Solid oxide fuel cell; SOFC; Nickel catalyst; YSZ support; Sulfur poisoning; Carbonyl sulfide; Sulfur; Poisoning
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