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The Effects of CO, H2, and C3H6 on the SCR Reactions of an Fe Zeolite SCR Catalyst University of Michigan

SAE Technical Papers (1906-current) Available online

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Format:
Conference/Event
Author/Creator:
Smith, Smith, author.
Contributor:
Assanis, Dennis N.
Bohac, Stani
Depcik, Christopher
Hoard, John
Conference Name:
SAE 2013 World Congress & Exhibition (2013-04-16 : Detroit, Michigan, United States)
Language:
English
Physical Description:
1 online resource
Place of Publication:
Warrendale, PA SAE International 2013
Summary:
Selective Catalytic Reduction (SCR) catalysts used in LeanNOx Trap (LNT) - SCR exhaust aftertreatment systemstypically encounter alternating oxidizing and reducingenvironments. Reducing conditions occur when diesel fuel isinjected upstream of a reformer catalyst, generating highconcentrations of hydrogen (H₂), carbon monoxide (CO), andhydrocarbons to deNOx the LNT. In this study, thefunctionality of an iron (Fe) zeolite SCR catalyst is explored witha bench top reactor during steady-state and cyclic transient SCRoperation.Experiments to characterize the effect of an LNTdeNOx event on SCR operation show that adding H₂ or COonly slightly changes SCR behavior with the primary contributionbeing an enhancement of nitrogen dioxide (NO₂) decomposition intonitric oxide (NO). Exposure of the catalyst to C₃H₆ (a surrogatefor an actual exhaust HC mixture) leads to a significant decreasein NOx reduction capabilities of the catalyst. Adegradation mechanism is proposed to account for the decrease inNOx conversion efficiency, highlighted by reactionsbetween NO₂ and C₃H₆ to make NO at a rate of similar order ofmagnitude as the Fast SCR reaction. This inhibits SCR reactionswhen the NO:NOx ratio favors NO, but can increaseNOx conversion when the NO:NOx ratio favorsNO₂.Ammonia (NH₃) storage is only marginally affected by thepresence of H₂, CO, or C₃H₆; but significant amounts of C₃H₆ can bestored on the catalyst. Further observation reveals that theoxidation effects of C₃H₆ are non-negligible and C₃H₆ stronglyinfluences the oxidation of NH₃. The degradation mechanism includesseven proposed reactions to model the experimental results ofadding H₂, CO, and C₃H₆ to the SCR feed gas during steady-state andtransient operation
Notes:
Vendor supplied data
Publisher Number:
2013-01-1062
Access Restriction:
Restricted for use by site license

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