SAE International Ammonia Generation and Utilization in a Passive SCR (TWC+SCR) System on Lean Gasoline Engine 2016-01-0934

Description
Lean gasoline engines offer greater fuel economy than the common stoichiometric gasoline engine, but the current three way catalyst (TWC) on stoichiometric engines is unable to control nitrogen oxide (NO X ) emissions in oxidizing exhaust. For these lean gasoline engines, lean NO X emission control is required to meet existing Tier 2 and upcoming Tier 3 emission regulations set by the U.S. Environmental Protection Agency (EPA). While urea-based selective catalytic reduction (SCR) has proven effective in controlling NO X from diesel engines, the urea storage and delivery components can add significant size and cost. As such, onboard NH 3 production via a passive SCR approach is of interest. In a passive SCR system, NH 3 is generated over a close-coupled TWC during periodic slightly rich engine operation and subsequently stored on an underfloor SCR catalyst. Upon switching to lean operation, NO X passes through the TWC and is reduced by the stored NH 3 on the SCR catalyst. In this work, a passive SCR system was evaluated on a 2.0-liter BMW lean burn gasoline direct injection engine to assess NH 3 generation over a Pd-only TWC and utilization over a Cu-based SCR catalyst. System NO X reduction efficiency and fuel efficiency improvement compared to stoichiometric engine operation were measured. A feedback control strategy based on cumulative NH 3 produced by the TWC during rich operation and NO X emissions during lean operation was implemented on the engine to control lean/rich cycle timing. At an SCR average inlet temperature of 350 °C, an NH 3 :NO X ratio of 1.15:1 (achieved through longer rich cycle timing) resulted in 99.7 % NO X conversion. Increasing NH 3 generation further resulted in even higher NO X conversion; however, tailpipe NH 3 emissions resulted. At higher underfloor temperatures, NH 3 oxidation over the SCR limited NH 3 availability for NO X reduction. At the engine conditions studied, greater than 99 % NO X conversion was achieved with passive SCR while delivering fuel efficiency benefits ranging between 6-11 % compared with stoichiometric operation.
Description
Lean gasoline engines offer greater fuel economy than the common stoichiometric gasoline engine, but the current three way catalyst (TWC) on stoichiometric engines is unable to control nitrogen oxide (NO X ) emissions in oxidizing exhaust. For these lean gasoline engines, lean NO X emission control is required to meet existing Tier 2 and upcoming Tier 3 emission regulations set by the U.S. Environmental Protection Agency (EPA). While urea-based selective catalytic reduction (SCR) has proven effective in controlling NO X from diesel engines, the urea storage and delivery components can add significant size and cost. As such, onboard NH 3 production via a passive SCR approach is of interest. In a passive SCR system, NH 3 is generated over a close-coupled TWC during periodic slightly rich engine operation and subsequently stored on an underfloor SCR catalyst. Upon switching to lean operation, NO X passes through the TWC and is reduced by the stored NH 3 on the SCR catalyst. In this work, a passive SCR system was evaluated on a 2.0-liter BMW lean burn gasoline direct injection engine to assess NH 3 generation over a Pd-only TWC and utilization over a Cu-based SCR catalyst. System NO X reduction efficiency and fuel efficiency improvement compared to stoichiometric engine operation were measured. A feedback control strategy based on cumulative NH 3 produced by the TWC during rich operation and NO X emissions during lean operation was implemented on the engine to control lean/rich cycle timing. At an SCR average inlet temperature of 350 °C, an NH 3 :NO X ratio of 1.15:1 (achieved through longer rich cycle timing) resulted in 99.7 % NO X conversion. Increasing NH 3 generation further resulted in even higher NO X conversion; however, tailpipe NH 3 emissions resulted. At higher underfloor temperatures, NH 3 oxidation over the SCR limited NH 3 availability for NO X reduction. At the engine conditions studied, greater than 99 % NO X conversion was achieved with passive SCR while delivering fuel efficiency benefits ranging between 6-11 % compared with stoichiometric operation.

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Ammonia Generation and Utilization in a Passive SCR (TWC+SCR) System on Lean Gasoline Engine - 2016-01-0934 - SAE International
Warrendale, PA, United States
Ammonia Generation and Utilization in a Passive SCR (TWC+SCR) System on Lean Gasoline Engine
2016-01-0934
Ammonia Generation and Utilization in a Passive SCR (TWC+SCR) System on Lean Gasoline Engine 2016-01-0934
Lean gasoline engines offer greater fuel economy than the common stoichiometric gasoline engine, but the current three way catalyst (TWC) on stoichiometric engines is unable to control nitrogen oxide (NO X ) emissions in oxidizing exhaust. For these lean gasoline engines, lean NO X emission control is required to meet existing Tier 2 and upcoming Tier 3 emission regulations set by the U.S. Environmental Protection Agency (EPA). While urea-based selective catalytic reduction (SCR) has proven effective in controlling NO X from diesel engines, the urea storage and delivery components can add significant size and cost. As such, onboard NH 3 production via a passive SCR approach is of interest. In a passive SCR system, NH 3 is generated over a close-coupled TWC during periodic slightly rich engine operation and subsequently stored on an underfloor SCR catalyst. Upon switching to lean operation, NO X passes through the TWC and is reduced by the stored NH 3 on the SCR catalyst. In this work, a passive SCR system was evaluated on a 2.0-liter BMW lean burn gasoline direct injection engine to assess NH 3 generation over a Pd-only TWC and utilization over a Cu-based SCR catalyst. System NO X reduction efficiency and fuel efficiency improvement compared to stoichiometric engine operation were measured. A feedback control strategy based on cumulative NH 3 produced by the TWC during rich operation and NO X emissions during lean operation was implemented on the engine to control lean/rich cycle timing. At an SCR average inlet temperature of 350 °C, an NH 3 :NO X ratio of 1.15:1 (achieved through longer rich cycle timing) resulted in 99.7 % NO X conversion. Increasing NH 3 generation further resulted in even higher NO X conversion; however, tailpipe NH 3 emissions resulted. At higher underfloor temperatures, NH 3 oxidation over the SCR limited NH 3 availability for NO X reduction. At the engine conditions studied, greater than 99 % NO X conversion was achieved with passive SCR while delivering fuel efficiency benefits ranging between 6-11 % compared with stoichiometric operation.

Lean gasoline engines offer greater fuel economy than the common stoichiometric gasoline engine, but the current three way catalyst (TWC) on stoichiometric engines is unable to control nitrogen oxide (NO X ) emissions in oxidizing exhaust. For these lean gasoline engines, lean NO X emission control is required to meet existing Tier 2 and upcoming Tier 3 emission regulations set by the U.S. Environmental Protection Agency (EPA). While urea-based selective catalytic reduction (SCR) has proven effective in controlling NO X from diesel engines, the urea storage and delivery components can add significant size and cost. As such, onboard NH 3 production via a passive SCR approach is of interest. In a passive SCR system, NH 3 is generated over a close-coupled TWC during periodic slightly rich engine operation and subsequently stored on an underfloor SCR catalyst. Upon switching to lean operation, NO X passes through the TWC and is reduced by the stored NH 3 on the SCR catalyst. In this work, a passive SCR system was evaluated on a 2.0-liter BMW lean burn gasoline direct injection engine to assess NH 3 generation over a Pd-only TWC and utilization over a Cu-based SCR catalyst. System NO X reduction efficiency and fuel efficiency improvement compared to stoichiometric engine operation were measured. A feedback control strategy based on cumulative NH 3 produced by the TWC during rich operation and NO X emissions during lean operation was implemented on the engine to control lean/rich cycle timing. At an SCR average inlet temperature of 350 °C, an NH 3 :NO X ratio of 1.15:1 (achieved through longer rich cycle timing) resulted in 99.7 % NO X conversion. Increasing NH 3 generation further resulted in even higher NO X conversion; however, tailpipe NH 3 emissions resulted. At higher underfloor temperatures, NH 3 oxidation over the SCR limited NH 3 availability for NO X reduction. At the engine conditions studied, greater than 99 % NO X conversion was achieved with passive SCR while delivering fuel efficiency benefits ranging between 6-11 % compared with stoichiometric operation.

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  SAE International
Product Category Standards and Technical Documents
Product Number 2016-01-0934
Product Name Ammonia Generation and Utilization in a Passive SCR (TWC+SCR) System on Lean Gasoline Engine
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