CLOSE-COUPLED SCR SYSTEM
A system for treating exhaust gases from a combustion engine and a method for using the same results in improved NO x conversion during engine startup. The system includes a compact SCR flow-through monolith installed upstream of a close-coupled SCR wall-flow filter, wherein the compact SCR flow-through monolith may be extruded or made of a thin-walled substrate, such that the SCR flow-through monolith has a smaller volume with lower heat capacity and higher catalyst loading relative to the SCR wall-flow filter.
1 . A system for treating exhaust gases containing NO x from an engine comprising:
a flow-through monolith having a first catalytic composition for selective catalytic reduction of NO x ;
a close-coupled particulate matter filter having a second catalytic composition for reduction of particulate matter and selective catalytic reduction of NO x ,
wherein said flow-through monolith is in fluid communication with, and incorporated upstream of, said close-coupled particulate matter filter,
wherein the flow-through monolith has a volume that is about 15% to about 40% of that of the close-coupled particulate matter filter,
wherein the first catalytic composition is present on the flow-through monolith at a first loading, the second catalytic composition is present on the close-coupled particulate matter filter at a second loading,
wherein the system does not comprise an oxidation catalyst upstream of the flow-through monolith, and
wherein the location of the close-coupled particulate matter filter relative to an upstream turbocharger is such that the exhaust gas travels less than 0.5 meters between the turbocharger and the close-coupled particulate matter filter.
2 . The system of claim 1 , wherein said flow-through monolith is an extruded catalyst brick.
3 . The system of claim 1 , wherein said close-coupled particulate matter filter is an inert substrate coated and/or impregnated with said second catalytic composition.
4 . The system of claim 3 , wherein said substrate is made primarily of either cordierite or metal.
5 . The system of claim 1 , wherein said flow-through monolith has a specific heat capacity that is about 35 to about 65% of the specific heat capacity of said particulate matter filter.
6 . The system of claim 1 , wherein said first and second catalytic compositions comprise a base-metal promoted aluminosilicate or silicoaluminophosphate molecular sieve.
7 . The system of claim 1 , wherein said flow-through monolith has an SCR catalyst loading of about 3 to 15 g/in 3 .
8 . The system of claim 1 , wherein said first and second catalytic compositions are different, provided that at least one of said first and second catalytic compositions comprise a base-metal promoted aluminosilicate or silicoaluminophosphate molecular sieve.
9 . The system of claim 1 , wherein said second catalytic composition for selective catalytic reduction of NO x is coated and/or impregnated on a downstream side of said close-coupled particulate matter filter.
10 . The system of claim 1 , wherein said second catalytic composition for selective catalytic reduction of NO x is coated and/or impregnated on an upstream side of said close-coupled particulate matter filter.
11 . The system of claim 1 , further comprising a source of reductant injection, in fluid communication with and disposed between said flow-through monolith and said close-coupled particulate matter filter.
12 . The system of claim 1 , wherein the first catalytic composition comprises an iron promoted zeolite and the second catalytic composition comprises a copper promoted zeolite.
13 . The system of claim 1 , further comprising a source of reductant injection, in fluid communication with and disposed between said flow-through monolith and said close-coupled particulate matter filter.
14 . The system of claim 1 , wherein the location of the close-coupled particulate matter filter relative to an upstream turbocharger is such that the exhaust gas travels less than 0.25 meters between the turbocharger and the close-coupled particulate matter filter.
15 . The system of claim 1 , wherein the flow-through monolith has an SCR catalyst loading of about 4 to 10 g/in 3 .
16 . The system of claim 1 , wherein the flow-through monolith has a volume that is about 20% to about 25% of that of the close-coupled particulate matter filter.