SAE International NO x Reduction with the Combinations on LNT and SCR in Diesel Applications 2013-24-0161

Description
Stricter emission limitations for NO x and particulates in mobile diesel applications will require the combinations of active aftertreatment methods like Diesel Particulate Filters (DPF), Selective Catalytic Reduction (SCR) with urea and Lean NO x Trap (LNT) in the 2010's. A new concept is the combination of LNT+SCR, which enables on-board synthesis of ammonia (LNT), which is then removed on the SCR catalyst. The main application for this kind system will be light-duty vehicles, where LNTs are already used and the low temperature deNO x is a main target. That combinatory system was investigated by developing and selecting PtRh/LNT and SCR catalysts for that particulate application, where the maximum temperature may reach 800°C and SCR should proceed without NO 2 assistance. Pt-rich, PtRh/LNT with reasonable high loadings above 80g/cft resulted in a high NO x efficiency in the experimental laboratory conditions which created also on LNTs a higher NH 3 concentration for the SCR unit. The SCR catalyst with copper as an active metal (Cu- SCR) showed the good durability up to 800°C and a wide operation window without the NO 2 assistance. Fe-SCR and VSCR catalysts were more dependent on NO 2 , which is not present after LNT and DPF. An optimized concept had an air injection after LNT to keep SCR condition always lean side, where the SCR reaction was promoted by oxygen with a high selectivity without NH 3 emissions. The simulations in reaction conditions and system design resulted in the proposals for the optimal design and main reaction mechanism.
Description
Stricter emission limitations for NO x and particulates in mobile diesel applications will require the combinations of active aftertreatment methods like Diesel Particulate Filters (DPF), Selective Catalytic Reduction (SCR) with urea and Lean NO x Trap (LNT) in the 2010's. A new concept is the combination of LNT+SCR, which enables on-board synthesis of ammonia (LNT), which is then removed on the SCR catalyst. The main application for this kind system will be light-duty vehicles, where LNTs are already used and the low temperature deNO x is a main target. That combinatory system was investigated by developing and selecting PtRh/LNT and SCR catalysts for that particulate application, where the maximum temperature may reach 800°C and SCR should proceed without NO 2 assistance. Pt-rich, PtRh/LNT with reasonable high loadings above 80g/cft resulted in a high NO x efficiency in the experimental laboratory conditions which created also on LNTs a higher NH 3 concentration for the SCR unit. The SCR catalyst with copper as an active metal (Cu- SCR) showed the good durability up to 800°C and a wide operation window without the NO 2 assistance. Fe-SCR and VSCR catalysts were more dependent on NO 2 , which is not present after LNT and DPF. An optimized concept had an air injection after LNT to keep SCR condition always lean side, where the SCR reaction was promoted by oxygen with a high selectivity without NH 3 emissions. The simulations in reaction conditions and system design resulted in the proposals for the optimal design and main reaction mechanism.

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NO x Reduction with the Combinations on LNT and SCR in Diesel Applications - 2013-24-0161 - SAE International
Warrendale, PA, United States
NO x Reduction with the Combinations on LNT and SCR in Diesel Applications
2013-24-0161
NO x Reduction with the Combinations on LNT and SCR in Diesel Applications 2013-24-0161
Stricter emission limitations for NO x and particulates in mobile diesel applications will require the combinations of active aftertreatment methods like Diesel Particulate Filters (DPF), Selective Catalytic Reduction (SCR) with urea and Lean NO x Trap (LNT) in the 2010's. A new concept is the combination of LNT+SCR, which enables on-board synthesis of ammonia (LNT), which is then removed on the SCR catalyst. The main application for this kind system will be light-duty vehicles, where LNTs are already used and the low temperature deNO x is a main target. That combinatory system was investigated by developing and selecting PtRh/LNT and SCR catalysts for that particulate application, where the maximum temperature may reach 800°C and SCR should proceed without NO 2 assistance. Pt-rich, PtRh/LNT with reasonable high loadings above 80g/cft resulted in a high NO x efficiency in the experimental laboratory conditions which created also on LNTs a higher NH 3 concentration for the SCR unit. The SCR catalyst with copper as an active metal (Cu- SCR) showed the good durability up to 800°C and a wide operation window without the NO 2 assistance. Fe-SCR and VSCR catalysts were more dependent on NO 2 , which is not present after LNT and DPF. An optimized concept had an air injection after LNT to keep SCR condition always lean side, where the SCR reaction was promoted by oxygen with a high selectivity without NH 3 emissions. The simulations in reaction conditions and system design resulted in the proposals for the optimal design and main reaction mechanism.

Stricter emission limitations for NO x and particulates in mobile diesel applications will require the combinations of active aftertreatment methods like Diesel Particulate Filters (DPF), Selective Catalytic Reduction (SCR) with urea and Lean NO x Trap (LNT) in the 2010's. A new concept is the combination of LNT+SCR, which enables on-board synthesis of ammonia (LNT), which is then removed on the SCR catalyst. The main application for this kind system will be light-duty vehicles, where LNTs are already used and the low temperature deNO x is a main target. That combinatory system was investigated by developing and selecting PtRh/LNT and SCR catalysts for that particulate application, where the maximum temperature may reach 800°C and SCR should proceed without NO 2 assistance. Pt-rich, PtRh/LNT with reasonable high loadings above 80g/cft resulted in a high NO x efficiency in the experimental laboratory conditions which created also on LNTs a higher NH 3 concentration for the SCR unit. The SCR catalyst with copper as an active metal (Cu- SCR) showed the good durability up to 800°C and a wide operation window without the NO 2 assistance. Fe-SCR and VSCR catalysts were more dependent on NO 2 , which is not present after LNT and DPF. An optimized concept had an air injection after LNT to keep SCR condition always lean side, where the SCR reaction was promoted by oxygen with a high selectivity without NH 3 emissions. The simulations in reaction conditions and system design resulted in the proposals for the optimal design and main reaction mechanism.

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  SAE International
Product Category Standards and Technical Documents
Product Number 2013-24-0161
Product Name NO x Reduction with the Combinations on LNT and SCR in Diesel Applications
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