Alumina-based lean NOx trap system and method of use
Abstract
An alumina-based lean NO x trap system for use in a lean burn engine such as a diesel engine is provided which includes at least one alumina-based lean NO x trap comprising a catalyst, an alumina NO x absorbent material, and optionally, from 0 to about 4 wt % of an alkaline earth metal oxide. The system preferably includes at least a first alumina-based lean NO x trap, and a second lean NO x trap which is positioned downstream from the first lean NO x trap in an engine exhaust. The second lean NO x trap may comprise an alumina-based trap or a conventional lean NO x trap. The lean NO x trap system converts at least a portion of NO x contained in the exhaust gas to N 2 at a temperature between about 150° C. to about 500° C. The alumina-based lean NO x trap system also undergoes efficient desulphurization and maintains its activity with extended use.
Claims
exact text as granted — not AI-modified1 . A lean NO x trap system for use in a lean burn engine exhaust comprising:
a first lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and optionally, an alkaline earth metal oxide; and a second lean NO x trap; wherein said system converts at least a portion of NO x contained in exhaust gas from said engine to N 2 at a temperature range of between about 150° C. to about 500° C.
2 . The system of claim 1 wherein said first lean NO x trap comprises from 0 to about 4.0 wt % of said alkaline earth metal oxide.
3 . The system of claim 1 wherein said second lean NO x trap comprises a catalyst, a NO x absorbent material comprising alumina, and optionally, from 0 to about 4 wt % an alkaline earth metal oxide.
4 . The system of claim 1 wherein said second lean NO x trap comprises a catalyst and from about 20 to 35 wt % of a metal oxide on an alumina or silica support.
5 . The system of claim 1 wherein said catalyst in said first lean NO x trap is selected from platinum, rhodium, and combinations thereof.
6 . The system of claim 1 having a conversion efficiency of at least 50% at a temperature between about 150° C. to about 500° C.
7 . The system of claim 1 wherein said first lean NO x trap further includes less than about 4 wt % of a stabilizing metal selected from La, Ce, and Ba.
8 . The system of claim 1 wherein said alkaline earth metal is selected from Mg, Sr, Ba, and Ca.
9 . The system of claim 1 further including a third lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and optionally, from 0 to about 4 wt % of an alkaline earth metal oxide.
10 . A lean NO x trap system for use in a lean burn engine exhaust comprising:
a first lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and from 0 to about 4.0 wt % of an alkaline earth metal oxide; and a second lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and from 0 to about 4.0 wt % of an alkaline earth metal oxide.
11 . The system of claim 10 wherein said second lean NO x trap is positioned downstream from said first lean NO x trap.
12 . The system of claim 10 further including a diesel particulate filter.
13 . The system of claim 10 further including a third lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and from 0 to about 4.0 wt % of an alkaline earth metal oxide.
14 . The system of claim 13 wherein said third lean NO x trap is positioned downstream from said second lean NO x trap.
15 . A method for treating lean burn engine exhaust gases comprising:
providing a lean NO x trap system in an exhaust gas passage of a lean burn engine, said system comprising at least first and second lean NO x traps; wherein said first lean NO x trap comprises a catalyst, a NO x absorbent material comprising alumina, and optionally, from 0 to about 4 wt % of an alkaline earth metal oxide; and exposing said lean NO x trap system to engine exhaust gas containing NO x such that at least a portion of said NO x contained in said exhaust gas is converted to N 2 at a temperature between about 150° C. to 500° C.
16 . The method of claim 15 wherein said system provides a conversion efficiency of at least 50% at a temperature between about 150° C. to about 500° C.
17 . The method of claim 16 wherein said engine exhaust gas is subjected to a fixed lean time/rich time ratio (x/y=R), and wherein the NO x conversion efficiency is increased by reducing x and y at a temperature of about 150 to 200° C.
18 . The method of claim 17 including sensing the concentration of NO x in said exhaust gas and adjusting the lean/rich cycle of said engine to increase said NO x conversion efficiency.
19 . The method of claim 15 wherein said NO x in said first lean NO x trap is converted at a temperature of between about 150° C. to about 350° C.
20 . The method of claim 15 wherein said NO x in said second lean NO x trap is converted at a temperature of between about 150° C. to about 350° C.
21 . The method of claim 15 wherein said second lean NO x trap is positioned downstream from said first lean NO x trap.
22 . The method of claim 15 wherein said first lean NO x trap is positioned downstream from said second lean NO x trap.
23 . The method of claim 15 wherein said first lean NO x trap and said second lean NO x trap are combined.
24 . The method of claim 15 wherein said second lean NO x trap comprises a catalyst, a NO x absorbent material comprising alumina, and optionally, from 0 to about 4 wt % of an alkaline earth metal oxide.
25 . The method of claim 15 wherein said second lean NO x trap comprises a catalyst and from about 20 to 35 wt % of a metal oxide on an alumina or silica support.
26 . A method for desulphurization of a lean NO x trap system in a lean burn engine comprising:
providing a lean NO x trap system including a first lean NO x trap comprising a catalyst, a NO x absorbent material comprising alumina, and optionally, an alkaline earth metal oxide; and a second lean NO x trap positioned downstream from said first lean NO x trap; said system being positioned in the exhaust passage of said engine such that it is exposed to exhaust gases therein; and heating said exhaust gases in said first lean NO x trap to a temperature of between about 550° C. and about 650° C. for at least 40 seconds.
27 . The method of claim 26 wherein said first lean NO x trap comprises from 0 to about 4 wt % of said alkaline earth metal oxide.
28 . The method of claim 26 wherein said second lean NO x trap comprises a catalyst, a NO x absorbent material comprising alumina, and optionally, from 0 to 4 wt % of an alkaline earth metal oxide.
29 . The method of claim 26 wherein said second lean NO x trap comprises a catalyst and from about 20 to 35 wt % of a metal oxide on an alumina or silica support.
30 . The method of claim 26 wherein said system further includes a bypass exhaust line for directing exhaust gas through said second lean NO x trap during normal vehicle operation but which diverts exhaust gas around said second lean NO x trap during desulphurization of said first lean NO x trap.
31 . The method of claim 26 wherein during desulphurization, λ is between about 0.98 to about 0.99.
32 . The method of claim 26 wherein said exhaust gases are heated for about 40 to 120 seconds.
33 . The method of claim 26 wherein said desulphurization of said lean NO x trap system produces a sulfur product comprising at least 90% SO 2 .Cited by (0)
No later patents cite this yet.
References (0)
No backward citations on record.