In this work, the effect of the soot-catalyst contact on the regeneration performance of a diesel particulate filter (DPF) wash-coated with nano-metric ceria particles was investigated. The catalyst load was suitably chosen to avoid major changes in pore size distribution of the original filter. Different amounts of soot were loaded into the filter, thus varying the catalyst/soot ratio. Filter samples were characterized by N-2 physisorption at 77 K, Hg intrusion porosimetry and SEM/EDX analysis. Regeneration tests, were performed in a lab-scale plant by temperature programmed combustion of soot.At the lowest soot load explored (corresponding to catalyst/soot ratio similar to 100w/w), the soot particles deeply penetrate into the macro-pores of the filter walls coming in close touch with highly dispersed ceria. At the highest soot load explored (catalyst/soot ratio similar to 20w/w), in addition to the soot particles trapped inside the macro-pores, a thick soot cake layer accumulates on top of the catalytic walls of the filter. The former condition results in a large fraction of soot burned, ia catalytic path (around 80%-almost purely catalytic regeneration mode) and, thus, in good regeneration performance (e.g., temperature at which 10% of the initial soot is converted, T-10%, equal to around 350 degrees C). Conversely, due to the poor cake catalyst contact, the latter condition results in a large fraction of soot burned via thermal path (around 80% catalyst-assisted thermal regeneration mode) and, thus, in much worse regeneration performance (e.g., T-10% similar to 475 degrees C).

Catalytic diesel particulate filters with highly dispersed ceria: Effect of the soot-catalyst contact on the regeneration performance

Di Sarli Valeria;Landi Gianluca;Lisi Luciana;
2016

Abstract

In this work, the effect of the soot-catalyst contact on the regeneration performance of a diesel particulate filter (DPF) wash-coated with nano-metric ceria particles was investigated. The catalyst load was suitably chosen to avoid major changes in pore size distribution of the original filter. Different amounts of soot were loaded into the filter, thus varying the catalyst/soot ratio. Filter samples were characterized by N-2 physisorption at 77 K, Hg intrusion porosimetry and SEM/EDX analysis. Regeneration tests, were performed in a lab-scale plant by temperature programmed combustion of soot.At the lowest soot load explored (corresponding to catalyst/soot ratio similar to 100w/w), the soot particles deeply penetrate into the macro-pores of the filter walls coming in close touch with highly dispersed ceria. At the highest soot load explored (catalyst/soot ratio similar to 20w/w), in addition to the soot particles trapped inside the macro-pores, a thick soot cake layer accumulates on top of the catalytic walls of the filter. The former condition results in a large fraction of soot burned, ia catalytic path (around 80%-almost purely catalytic regeneration mode) and, thus, in good regeneration performance (e.g., temperature at which 10% of the initial soot is converted, T-10%, equal to around 350 degrees C). Conversely, due to the poor cake catalyst contact, the latter condition results in a large fraction of soot burned via thermal path (around 80% catalyst-assisted thermal regeneration mode) and, thus, in much worse regeneration performance (e.g., T-10% similar to 475 degrees C).
2016
Istituto di Ricerche sulla Combustione - IRC - Sede Napoli
Catalytic diesel particulate filters
Soot
Catalyst dispersion
Soot-catalyst contact
Ceria
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Utilizza questo identificativo per citare o creare un link a questo documento: https://hdl.handle.net/20.500.14243/314971
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