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Deactivation of Pd Catalysts by Water during Low Temperature Methane Oxidation Relevant to Natural Gas Vehicle Converters Gholami, Rahman; Alyani, Mina; Smith, Kevin J.
Abstract
Effects of H₂O on the activity and deactivation of Pd catalysts used for the oxidation of unburned CH₄ present in the exhaust gas of natural-gas vehicles (NGVs) are reviewed. CH₄ oxidation in a catalytic converter is limited by low exhaust gas temperatures (500–550 °C) and low concentrations of CH₄ (400–1500 ppmv) that must be reacted in the presence of large quantities of H₂O (10–15%) and CO₂ (15%), under transient exhaust gas flows, temperatures, and compositions. Although Pd catalysts have the highest known activity for CH₄ oxidation, water-induced sintering and reaction inhibition by H₂O deactivate these catalysts. Recent studies have shown the reversible inhibition by H₂O adsorption causes a significant drop in catalyst activity at lower reaction temperatures (below 450 °C), but its effect decreases (water adsorption becomes more reversible) with increasing reaction temperature. Thus above 500 °C H₂O inhibition is negligible, while Pd sintering and occlusion by support species become more important. H₂O inhibition is postulated to occur by either formation of relatively stable Pd(OH)₂ and/or partial blocking by OH groups of the O exchange between the support and Pd active sites thereby suppressing catalytic activity. Evidence from FTIR and isotopic labeling favors the latter route. Pd catalyst design, including incorporation of a second noble metal (Rh or Pt) and supports high O mobility (e.g., CeO₂) are known to improve catalyst activity and stability. Kinetic studies of CH₄ oxidation at conditions relevant to natural gas vehicles have quantified the thermodynamics and kinetics of competitive H₂O adsorption and Pd(OH)₂ formation, but none have addressed effects of H₂O on O mobility.
Item Metadata
Title |
Deactivation of Pd Catalysts by Water during Low Temperature Methane Oxidation Relevant to Natural Gas Vehicle Converters
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Creator | |
Publisher |
Multidisciplinary Digital Publishing Institute
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Date Issued |
2015-03-31
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Description |
Effects of H₂O on the activity and deactivation of Pd catalysts used for the oxidation of unburned CH₄ present in the exhaust gas of natural-gas vehicles (NGVs) are reviewed. CH₄ oxidation in a catalytic converter is limited by low exhaust gas temperatures (500–550 °C) and low concentrations of CH₄ (400–1500 ppmv) that must be reacted in the presence of large quantities of H₂O (10–15%) and CO₂ (15%), under transient exhaust gas flows, temperatures, and compositions. Although Pd catalysts have the highest known activity for CH₄ oxidation, water-induced sintering and reaction inhibition by H₂O deactivate these catalysts. Recent studies have shown the reversible inhibition by H₂O adsorption causes a significant drop in catalyst activity at lower reaction temperatures (below 450 °C), but its effect decreases (water adsorption becomes more reversible) with increasing reaction temperature. Thus above 500 °C H₂O inhibition is negligible, while Pd sintering and occlusion by support species become more important. H₂O inhibition is postulated to occur by either formation of relatively stable Pd(OH)₂ and/or partial blocking by OH groups of the O exchange between the support and Pd active sites thereby suppressing catalytic activity. Evidence from FTIR and isotopic labeling favors the latter route. Pd catalyst design, including incorporation of a second noble metal (Rh or Pt) and supports high O mobility (e.g., CeO₂) are known to improve catalyst activity and stability. Kinetic studies of CH₄ oxidation at conditions relevant to natural gas vehicles have quantified the thermodynamics and kinetics of competitive H₂O adsorption and Pd(OH)₂ formation, but none have addressed effects of H₂O on O mobility.
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Subject | |
Genre | |
Type | |
Language |
eng
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Date Available |
2019-04-16
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Provider |
Vancouver : University of British Columbia Library
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Rights |
CC BY 4.0
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DOI |
10.14288/1.0378246
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URI | |
Affiliation | |
Citation |
Catalysts 5 (2): 561-594 (2015)
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Publisher DOI |
10.3390/catal5020561
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Peer Review Status |
Reviewed
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Scholarly Level |
Faculty
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Rights URI | |
Aggregated Source Repository |
DSpace
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Item Media
Item Citations and Data
Rights
CC BY 4.0