Catalytic combustion of ventilation air methane (VAM) – long term catalyst stability in the presence of water vapour and mine dust
Author(s) -
Adi Setiawan,
Jarrod Friggieri,
Eric M. Kennedy,
Bogdan Z. Dlugogorski,
Michael Stockenhuber
Publication year - 2014
Publication title -
catalysis science and technology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 1.635
H-Index - 115
eISSN - 2044-4761
pISSN - 2044-4753
DOI - 10.1039/c4cy00120f
Subject(s) - catalysis , methane , combustion , environmental science , waste management , water vapor , catalytic combustion , durability , ventilation (architecture) , coal , coal dust , chemistry , environmental engineering , chemical engineering , materials science , engineering , composite material , organic chemistry , mechanical engineering
In this paper, we report new insights into the deactivation phenomenon of palladium based catalysts for catalytic combustion of ventilation air methane (VAM). It was found that the primary factor responsible for low temperature catalyst deactivation is the water vapour present in the feed stream. The influence of water vapour on VAM was examined by comparing the properties of fresh catalysts with catalysts following over 1000 h reaction time-on-stream. The techniques applied to characterize the catalysts included TPD, XRD, N₂-isotherm adsorption, H₂-chemisorption and XPS analyses. Alternating between dry and water vapour-saturated VAM feed disclosed ca. 50% reversible drop in activity. XPS analysis suggests an absence of a palladium hydroxide phase during the initial 2 h on stream, although prolonged exposure to the reactant leads to the formation of palladium hydroxide, which appears to match the progressive deactivation of the Pd/Al₂O₃catalyst. Introduction of VAM dust (a mixture of fine coal, CaCO₃and aluminosilicate particles) causes a variation in catalytic activity originating from coal-dust ignition and the effect of chloride on the surface of the catalyst. In the presence of these inhibiting agents, an average methane conversion of higher than 75% over 1100 h was achieved at reaction temperatures below 600°C
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