U.S. patent application number 11/298814 was filed with the patent office on 2006-08-03 for alumina-based lean nox trap system and method of use in dual-mode hcci engines.
Invention is credited to George Graham, Lifeng Xu, Jialin Yang.
Application Number | 20060168949 11/298814 |
Document ID | / |
Family ID | 36755038 |
Filed Date | 2006-08-03 |
United States Patent
Application |
20060168949 |
Kind Code |
A1 |
Xu; Lifeng ; et al. |
August 3, 2006 |
Alumina-based lean NOx trap system and method of use in dual-mode
HCCI engines
Abstract
An alumina-based lean NO.sub.x trap system for use in a HCCI
engine exhaust is provided which includes at least one
alumina-based lean NO.sub.x trap comprising a catalyst, an alumina
NO.sub.x absorbent material, and optionally, from 0 to about 4 wt %
of an alkaline earth metal oxide; and a conventional three-way
catalyst. The lean NO.sub.x trap system substantially oxidizes HC
and CO and converts at least a portion of NO.sub.x contained in the
exhaust gas to N.sub.2 at a temperature between about 150.degree.
C. to about 250.degree. C. in HCCI mode. The system also
effectively removes HC, CO and NO.sub.x at high temperature when
the engine is in SI mode (stoichiometric conditions). The
alumina-based lean NO.sub.x trap in the system also undergoes
efficient desulphurization and maintains its activity with extended
use.
Inventors: |
Xu; Lifeng; (Farmington
Hills, MI) ; Yang; Jialin; (Canton, MI) ;
Graham; George; (Ann Arbor, MI) |
Correspondence
Address: |
DINSMORE & SHOHL LLP;One Dayton Centre
Suite 1300
One South Main Street
Dayton
OH
45402-2023
US
|
Family ID: |
36755038 |
Appl. No.: |
11/298814 |
Filed: |
December 9, 2005 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
60649331 |
Feb 2, 2005 |
|
|
|
Current U.S.
Class: |
60/295 ;
60/301 |
Current CPC
Class: |
F01N 3/0842 20130101;
F02D 41/0275 20130101; Y02T 10/24 20130101; F01N 3/0814 20130101;
B01D 2255/1025 20130101; B01D 2255/204 20130101; B01D 2255/91
20130101; Y02T 10/128 20130101; B01D 53/9422 20130101; F01N 2370/02
20130101; Y02T 10/22 20130101; F02D 41/3035 20130101; F01N 13/009
20140601; B01D 2255/1021 20130101; B01D 53/945 20130101; F01N
13/0097 20140603; F01N 13/0093 20140601; Y02T 10/12 20130101; F02D
41/028 20130101 |
Class at
Publication: |
060/295 ;
060/301 |
International
Class: |
F01N 3/10 20060101
F01N003/10; F01N 3/00 20060101 F01N003/00 |
Claims
1. A lean NO.sub.x trap system for use in a HCCI engine exhaust
comprising: a first lean NO.sub.x trap comprising a catalyst, a
NO.sub.x absorbent material comprising alumina, and optionally,
from 0 to about 4 wt % of an alkaline earth metal oxide; and a
three-way catalyst; wherein said system oxidizes HC and CO and
converts at least a portion of NO.sub.x contained in exhaust gas
from said engine to N.sub.2 at a temperature range of between about
150.degree. C. to about 250.degree. C.
2. The system of claim 1 wherein said catalyst in said lean
NO.sub.x trap is selected from platinum, rhodium, and combinations
thereof.
3. The system of claim 1 having a NO.sub.x conversion efficiency of
at least 50% at a temperature between about 150.degree. C. to about
250.degree. C.
4. The system of claim 1 having a HC and CO conversion efficiency
of at least 70% at a temperature between about 150.degree. C. to
about 250.degree. C.
5. The system of claim 1 wherein said catalyst in said first lean
NO.sub.x trap is selected from platinum, rhodium, and combinations
thereof.
6. The system of claim 1 wherein said alkaline earth metal in said
metal oxide is selected from Mg, Sr, Ba, and Ca.
7. The system of claim 1 wherein said lean NO.sub.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 three-way catalyst is
positioned downstream from said lean NO.sub.x trap.
9. The system of claim 1 wherein said lean NO.sub.x trap and said
three-way catalyst are combined.
10. The system of claim 1 further including a second lean NO.sub.x
trap comprising a catalyst, a NO.sub.x absorbent material
comprising alumina, and optionally, from 0 to 4 wt % of an alkaline
earth metal oxide.
11. The system of claim 10 wherein said second lean NO.sub.x trap
is positioned downstream from said three-way catalyst.
12. A method for treating HCCI engine exhaust gases comprising:
providing a lean NO.sub.x trap system in an exhaust gas passage of
a HCCI engine said system comprising a first lean NO.sub.x trap
comprising a catalyst, a NO.sub.x absorbent material comprising
alumina, and optionally, from 0 to about 4 wt % of an alkaline
earth metal oxide; and a three-way catalyst; exposing said lean
NO.sub.x trap system to HCCI engine exhaust gas containing NO.sub.x
such that HC and CO are substantially oxidized, and at least a
portion of said NO.sub.x contained in said exhaust gas is converted
to N.sub.2 at a temperature between about 150.degree. C. to
250.degree. C.
13. The method of claim 12 wherein said three-way catalyst is
positioned downstream from said first lean NO.sub.x trap.
14. The method of claim 12 wherein said first lean NO.sub.x trap is
positioned downstream from said three-way catalyst.
15. The method of claim 12 wherein said first lean NO.sub.x trap
and said three-way catalyst are combined.
16. The method of claim 12 wherein said system includes a second
lean NO.sub.x trap positioned downstream from said three-way
catalyst, said second lean NO.sub.x trap comprising a catalyst, a
NO.sub.x absorbent material comprising alumina, and optionally,
from 0 to about 4 wt % of an alkaline earth metal oxide.
17. A method for desulphurization of a lean NO.sub.x trap system in
a HCCI engine comprising: providing a lean NO.sub.x trap system
including a first lean NO.sub.x trap comprising a catalyst, a
NO.sub.x absorbent material comprising alumina, and optionally,
from 0 to about 4 wt % of an alkaline earth metal oxide; and a
three-way catalyst positioned downstream from said first lean
NO.sub.x trap; said system being positioned in the exhaust passage
of said HCCI engine such that it is exposed to exhaust gases
therein; and heating said exhaust gases to a temperature of between
about 550 and 650.degree. C. for at least 60 seconds by operating
said engine in SI mode.
18. The method of claim 17 wherein said desulphurization of said
lean NO.sub.x trap system produces a sulfur product comprising at
least 90% SO.sub.2.
19. The method of claim 17 wherein during said desulphurization, x
is between 0.98 and 0.99.
Description
CROSS REFERENCE TO RELATED APPLICATIONS
[0001] This application claims the benefit of U.S. Provisional
Application No. 60/649,331, entitled SYSTEM FOR TREATING EMISSIONS
FROM DIESEL EXHAUST GAS, filed Feb. 2, 2005. The entire contents of
said application are hereby incorporated by reference.
BACKGROUND OF THE INVENTION
[0002] The present invention relates to a lean NO.sub.x trap system
for treating emissions from dual-mode HCCI engines, and more
particularly, to a system including at least one lean NO.sub.x trap
which utilizes alumina as a NO.sub.x storage material. The
alumina-based lean NO.sub.x trap achieves high NO.sub.x, HC and CO
conversion efficiencies at the low temperatures encountered in the
lean exhaust gas of HCCI engines. In addition, the alumina-based
lean NO.sub.x trap maintains its activity with extended use and
undergoes efficient desulphurization.
[0003] Government regulations, created in response to environmental
and health concerns, have necessitated the treatment of exhaust gas
from vehicle engines in order to reduce the level of certain
combustion by-products, including carbon monoxide (CO),
hydrocarbons (HC), and nitrogen oxides (NO.sub.x). In conventional
gasoline engines (i.e., engines that operate at a stoichiometric
air-to-fuel ratio), such treatment generally includes the use of a
three-way catalyst (TWC). In recent years, the development of HCCI
(homogeneous-charge-compression-ignition) engines has been found to
have the potential to significantly improve fuel efficiency (up to
50%) over conventional gasoline engines which operate in an SI
(spark-ignition) mode. In such engines, the charge is
compression-ignited, and the engine runs in very lean conditions
(.lamda. from about 30 to 80, where .lamda. represents the actual
air/fuel ratio divided by the stoichiometric air/fuel ratio), or in
highly diluted conditions (very large residual gas fraction), which
provides high efficiency, low emissions of NO.sub.x, and low cost
when compared with a diesel engine.
[0004] However, at high loads, operation of the engine in HCCI mode
is difficult. Accordingly, it is common for the HCCI engine to
employ both SI and HCCI combustion mode technology (referred to
herein as HCCI-SI, or dual-mode), which allows the engine to
operate in HCCI mode to achieve high fuel efficiency and low
NO.sub.x emissions at low and medium loads, and then switch to SI
mode at higher loads.
[0005] However, such a dual-mode engine requires a treatment system
for emissions in order to meet future emission regulations. When
the dual-mode engine is in SI mode, it is relatively easy to reduce
emissions with the use of a conventional three-way catalyst due to
the high exhaust temperature (about 450 to 600.degree. C.) and
stoichiometric air/fuel ratio in the exhaust gas. In the SI mode,
such a three-way catalyst is effective in reducing HC, CO and
NO.sub.x.
[0006] However, during HCCI mode, the exhaust temperature is low,
ranging from about 150 to 250.degree. C. (engine out temperature is
from about 190 to 300.degree. C.), and the exhaust gas is very
lean. A three-way catalyst cannot effectively reduce the level of
NO.sub.x, CO and HC under these conditions. In addition, the engine
exhaust has a large variation, with NO.sub.x ranging from 2 to 150
ppm, CO from 300 to 6000 ppm, and HC from 1000 to 4000 ppm. Thus,
when the engine operates in HCCI mode, a treatment system is needed
which can operate efficiently at low temperatures (150 to
250.degree. C.) to oxidize HC, CO and to reduce NO.sub.x (when
NO.sub.x concentration is higher than a certain threshold level)
under lean conditions.
[0007] Lean NO.sub.x traps (LNTs), which conventionally include a
catalyst comprising one or more precious metals and an alkaline
earth metal oxide provided on a support material such as alumina,
are known for use in lean-burn engines. Such LNTs are capable of
absorbing or storing nitrogen oxides during lean-burn engine
operation. Periodically, engine operation changes in order to
release and reduce NO.sub.x to nitrogen when the exhaust gas is in
rich condition. However, conventional lean NO.sub.x traps currently
in use are most effective at an operating temperature range of
about 200.degree. C. to about 500.degree. C., while the exhaust gas
temperature (catalyst inlet) during HCCI mode is typically less
than 200.degree. C. Thus, a conventional LNT cannot remove NO.sub.x
in HCCI exhaust gas.
[0008] Another disadvantage of conventional LNTs is that they
become poisoned over time by the accumulation of sulfur (SO.sub.x)
on the LNT due to combustion of the sulfur contained in the fuel.
Accordingly, it is necessary to perform a periodic (about every
5,000 miles) desulphurization (de-SO.sub.x) procedure to maintain
the activity and effectiveness of the trap. However,
desulphurization of a conventional LNT requires high temperatures
(650.degree. C. to 800.degree. C.) for relatively long times (5 to
10 minutes). This thermally damages the conventional LNT with each
de-SO.sub.x cycle, which reduces the activity of the LNT. In
addition, the de-SO.sub.x process results in a considerable fuel
consumption penalty (up to 5%).
[0009] Accordingly, there is still a need in the art for a system
of treating exhaust emissions from a dual-mode HCCI engine which
provides effective treatment at the lower temperatures encountered
during the HCCI mode of the engine, which maintains its activity
with extended use, and which undergoes efficient
desulphurization.
SUMMARY OF THE INVENTION
[0010] The present invention meets those needs by providing a lean
NO.sub.x trap (LNT) system for use in a dual-mode HCCI engine which
includes at least one lean NO.sub.x trap which utilizes alumina as
a NO.sub.x storage (absorbent) material. The alumina-based LNT,
when incorporated in a HCCI engine exhaust system along with a
conventional three-way catalyst, effectively converts HC, CO and
NO.sub.x at the low temperatures (about 150.degree. C.) encountered
during the HCCI operational mode of such engines. In addition, the
alumina-based LNT system functions as an oxidation catalyst in the
HCCI engine exhaust and provides effective oxidation of HC and CO
(above 90%) at low exhaust temperature. Further, the alumina-based
LNT maintains its activity with extended use and undergoes
efficient desulphurization.
[0011] When the engine operates in SI mode, the engine exhaust gas
is at stoichiometric conditions with high temperatures (500 to
600.degree. C.), and the gas includes all three pollutants (HC, CO
and NO.sub.x). For such conditions, the three-way catalyst in the
lean NO.sub.x trap system of the present invention effectively
converts these pollutants.
[0012] According to one aspect of the present invention, a lean
NO.sub.x trap system for use in a HCCI engine is provided. The
system comprises a first lean NO.sub.x trap comprising a catalyst,
a NO.sub.x absorbent material comprising alumina, and optionally,
from 0 to 4 wt % of an alkaline earth metal oxide (also referred to
herein as an alumina-based LNT); and a three-way catalyst.
[0013] The lean NO.sub.x trap system oxidizes HC and CO, and
converts at least a portion of NO.sub.x contained in lean exhaust
gas from the engine exhaust to N.sub.2 at a temperature range of
between about 150.degree. C. to about 250.degree. C. The system
preferably has a NO.sub.x conversion efficiency of at least 50% at
a temperature between about 150.degree. C. to about 250.degree. C.
In addition, the system has a conversion efficiency for HC and CO
of at least 70% in lean conditions at a temperature between about
150.degree. C. to about 250.degree. C. By conversion efficiency, it
is meant the difference between the levels of NO.sub.x, HC and CO
entering the trap and leaving the trap divided by the level
entering the trap, multiplied by 100%.
[0014] Preferably, the alumina-based lean NO.sub.x trap comprises
from 0 to about 4.0 wt % of the alkaline earth metal oxide, which
is preferably selected from Mg, Sr, Ba, and Ca.
[0015] The catalyst in the alumina-based LNT is preferably selected
from platinum, rhodium, and combinations thereof. The alumina-based
lean NO.sub.x trap preferably further includes less than about 4 wt
% of a stabilizing metal selected from La, Ce, and Ba.
[0016] In the system of the present invention, the three-way
catalyst is preferably positioned downstream from the lean NO.sub.x
trap. Alternatively, the alumina-based lean NO.sub.x trap and the
three-way catalyst may be combined.
[0017] In an alternative embodiment of the invention, a second
alumina-based lean NO.sub.x trap may be included in the system. In
this embodiment, the second alumina-based lean NO.sub.x trap is
positioned downstream from the three-way catalyst.
[0018] The present invention further provides a method for treating
HCCI engine exhaust gases which comprises providing a lean NO.sub.x
trap system in an exhaust gas passage of a HCCI engine, where the
system comprises a first lean NO.sub.x trap comprising a catalyst,
a NO.sub.x absorbent material comprising alumina, and optionally,
from 0 to 4.0 wt % of an alkaline earth metal oxide; and a
three-way catalyst.
[0019] The lean NO.sub.x trap system is exposed to lean HCCI engine
exhaust gas containing HC, CO, and NO.sub.x such that the HC and CO
is substantially oxidized and at least a portion of the NO.sub.x
contained in the exhaust gas is converted to N.sub.2 at a
temperature between about 150.degree. C. to 250.degree. C. By
"substantially oxidized," it is meant that at least 85% of the HC
and CO is oxidized.
[0020] It should be noted that when the lean NO.sub.x trap system
is exposed to SI engine exhaust gas (stoichiometric) containing HC,
CO and NO.sub.x, the HC, CO and NO.sub.x are converted to H.sub.2O,
CO.sub.2 and N.sub.2 at a temperature above about 450.degree. C.
During the transition of HCCI mode to SI mode, this system can
oxidize HC and CO at low temperature (<350.degree. C.) and raise
the temperature of the exhaust gas to shorten the light-off time of
the downstream three-way catalyst.
[0021] In one embodiment of the method, the three-way catalyst is
positioned downstream from the first lean NO.sub.x trap. In another
embodiment, the first lean NO.sub.x trap is positioned downstream
from the three-way catalyst. In yet another embodiment, the lean
NO.sub.x trap and three-way catalyst are combined. In yet another
embodiment of the method, a second alumina-based lean NO.sub.x trap
is included in the system which is positioned downstream from the
three-way catalyst.
[0022] The present invention also provides a method for
desulphurization of an alumina-based lean NO.sub.x trap system used
in a HCCI engine, where the system comprises at least one lean
NO.sub.x trap comprising a catalyst, a NO.sub.x absorbent material
comprising alumina, and optionally, from 0 to about 4.0 wt % of an
alkaline earth metal oxide, and a three-way catalyst.
[0023] In the desulphurization method, the LNT system is exposed to
exhaust gases in the HCCI engine. The exhaust gases are heated to a
temperature of between about 550 and 650.degree. C. for at least 60
seconds by operating the engine in SI mode. Preferably, during
desulphurization, .lamda. is between about 0.98 and 0.99. The
desulphurization of the lean NO.sub.x trap system causes the
alumina-based lean NO.sub.x trap to release a sulfur product
comprising at least 90% SO.sub.2. In addition, the alumina-based
lean NO.sub.x trap maintains its activity after the
desulphurization process.
[0024] Accordingly, it is a feature of the present invention to
provide a lean NO.sub.x trap system including an alumina-based lean
NO.sub.x trap which operates effectively at the low temperatures
and lean conditions encountered in the HCCI operational mode of
dual-mode HCCI engines, which maintains its activity over time, and
which undergoes efficient desulphurization. It is a further feature
of the invention to provide a lean NO.sub.x trap system including a
three-way catalyst which operates effectively at the high
temperatures and stoichiometric conditions encountered in the SI
operational mode of dual-mode HCCI engines. Other features and
advantages will be apparent from the following description and the
accompanying drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0025] FIG. 1 is a schematic illustration of the system of the
present invention including an alumina-based LNT and a conventional
three-way catalyst;
[0026] FIG. 2 is a schematic illustrations of the system including
a first alumina-based LNT and a three-way catalyst which are
combined on a single brick; and
[0027] FIG. 3 is a schematic illustration of the system including
first and second alumina-based LNTs and a three-way catalyst;
and
[0028] FIG. 4 is a graph illustrating the desulphurization
(de-SO.sub.x) performance of system of the present invention
including the alumina-based LNT and a three-way catalyst at
650.degree. C. and .lamda.=0.984.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
[0029] We have found that the use of alumina as a NO.sub.x storage
(absorbent) material in a lean NO.sub.x trap provides more
efficient release of NO.sub.x at low temperatures than conventional
lean NO.sub.x traps which utilize alkali metal oxides or alkaline
earth metal oxides as NO.sub.x storage materials. Because alkali
metals and alkaline earth metals are very basic in nature, such
storage materials have a strong interaction with NO.sub.x, which
interaction takes place at higher temperatures. As alumina has a
relatively weak interaction with NO.sub.x, it can absorb and
release NO.sub.x at much lower temperatures. While alumina has been
widely used in conventional LNTs as a support material for
catalysts, such LNTs include large amounts (e.g., about 20 to 35 wt
%) of alkali metal oxides and/or alkaline earth metal oxides. Such
large amounts of metal oxides dominate the NO.sub.x absorption
properties of the LNT, thus determining the activity of the LNT and
its other properties, i.e., operating temperature window,
de-SO.sub.x temperature, etc.
[0030] We have found that the use of an alumina-based lean NO.sub.x
trap system including at least one alumina-based trap containing
little or no alkaline earth metal oxides allows the alumina to
dominate the NO.sub.x absorption properties of the lean NO.sub.x
trap, resulting in high NO.sub.x conversion efficiency at
relatively low temperatures, e.g., about 150.degree. C. to
200.degree. C. The alumina-based LNT is also resistant to
degradation by aqueous-based processes previously found to cause
conventional traps to lose a substantial fraction of their initial
NO.sub.x storage capacity. The catalysts (Pt, Rh, etc.) in the
alumina-based LNT also function as very good HC and CO oxidation
catalysts in lean conditions to remove HC and CO at low
temperatures (above 150.degree. C.).
[0031] In addition, we have found that because the alumina-based
LNT has very strong oxidation capability at low temperatures, it
can shorten the light-off time for the three-way catalyst when the
engine operation transits from HCCI mode (<200.degree. C.) to SI
mode (about 500 to 600.degree. C.) by burning off the HC and CO and
raising the exhaust temperature before the three-way catalyst
lights off downstream from the LNT.
[0032] Desulphurization (de-SO.sub.x) of the alumina-based LNT
system is also achieved more efficiently than in a conventional LNT
as desulphurization can take place at lower temperatures for much
shorter periods of time. The alumina-based LNT system of the
present invention is resistant to SO.sub.2 poisoning since the
alumina-based LNT does not degrade when subjected to the
desulphurization process. Also, production of unwanted H.sub.2S
during desulphurization is minimized.
[0033] The alumina-based lean NO.sub.x trap of the present
invention is preferably prepared by coating a cordierite monolith
with a catalyst washcoat (about 5 to 7 kg/ft.sup.3) comprising from
about 95 to 99% by weight alumina Optionally, a stabilizing metal
comprising less than about 4% by weight of the total washcoat may
be added to stabilize the alumina surface area during the high
temperature exposure and to increase the durability of the LNT.
Suitable stabilizing metals include La, Ce, and Ba.
[0034] In addition, the alumina-based lean NO.sub.x trap optionally
includes from 0 to about 4.0% by weight of the total washcoat of an
alkaline earth metal oxide. Preferred alkaline earth metals include
Mg, Sr, Ba, and Ca. The alkaline earth metal oxide may be included
in the LNT for the purpose of shifting the operating temperature
window of the LNT, for example, to achieve higher operating
temperatures.
[0035] We have found that the addition of such a small amount of an
alkaline earth metal oxide (i.e., less than about 4.0 wt %) does
not impact the basic properties of the alumina-based LNT, e.g.,
high NO.sub.x conversion efficiency at low temperatures and
efficient desulphurization of the LNT. The alkaline earth metal
oxide may be added to the washcoat by a conventional aqueous
solution ion exchange method. For example, the alumina coated
monolith is ion exchanged from one to four times with an aqueous
solution of Ca cation. In the present invention, a
(Ca(NO.sub.3).sub.2 solution is preferred. The ion exchanges are
preferably carried out at room temperature with solutions of 0.5
mol/l. After each solution ion exchange step, the coated monolith
is preferably washed, dried, and calcined at about 773.degree. K
for about 4 hours prior to performing the next ion exchange
step.
[0036] Precious metal catalysts are then added to the washcoated
monolith. Preferred for use in the present invention are Pt and Rh,
which may be added at loadings of about 100 g Pt/ft.sup.3 and 20 g
Rh/ft.sup.3. The precious metals are loaded onto the alumina coated
monolith by the Subtractive Deposition Method, which includes 1)
measuring the volume of the monolith and calculating the amount
(Mp) of precious metal compound (e.g. H.sub.2PtCl.sub.6) needed for
the monolith to reach a certain precious metal loading (e.g. 100 g
Pt/ft.sup.3); 2) measuring the total volume (V.sub.H2O) of water
than can be absorbed by the washcoat onto the monolith at room
temperature; 3) preparing a solution of the precious metal compound
with the concentration Mp/V.sub.H2O; 4) dipping the monolith into
the prepared solution with a total volume of 2.5 times V.sub.H2O at
room temperature, wetting the monolith thoroughly, blowing away the
residual solution and drying the monolith at 130.degree. C. for 1
hour; and 5) where the precious metal compounds contain chlorine,
removing the chlorine (Cl) at 500.degree. C. in a flow reactor with
a mixed gas of 1% H.sub.2 and 10% H.sub.2O balanced by nitrogen for
4 hours. Where more than one precious metal is loaded onto the same
monolith, the procedure is repeated.
[0037] The three-way catalyst included in the system is preferably
a conventional three-way catalyst which is well known in the art
and typically comprises Pt, Pd and Rh on an alumina or silica
support.
[0038] Referring now to FIG. 1, the lean NO.sub.x trap system 10 of
the present invention is illustrated, which, in a preferred
embodiment, includes an alumina-based lean NO.sub.x trap 12 and a
three-way catalyst 14. The system is preferably coupled to the HCCI
engine such that exhaust gases flow through an exhaust manifold
into the system 10.
[0039] As shown, the three-way catalyst is positioned downstream
from the alumina-based lean NO.sub.x trap. Alternatively, the
alumina-based lean NO.sub.x trap may be positioned downstream from
the three-way catalyst. In yet another alternative embodiment, the
alumina-based trap and the three-way catalyst may be combined on a
single brick 16 as shown in FIG. 2. This may be achieved by coating
a single catalyst brick with two different compositions, i.e., the
alumina-based LNT composition and a conventional three-way catalyst
composition. In the embodiment shown, the alumina-based LNT is
positioned in front of the three-way catalyst; however, it should
be appreciated that the three-way catalyst may also be positioned
in front of the alumina-based LNT.
[0040] Referring now to FIG. 3, an alternative embodiment of the
invention is illustrated in which the system comprises first and
second alumina-based lean NO.sub.x traps (12, 18) in addition to a
three-way catalyst 14, where the second lean NO.sub.x trap is
positioned downstream from the three-way catalyst.
[0041] In use, the system of the present invention including at
least one alumina-based LNT is placed in the exhaust of a vehicle
having a HCCI engine. The system is exposed to the exhaust gas such
that HC and CO contained in the gas is oxidized and at least a
portion of the NO.sub.x in the gas is converted to N.sub.2,
preferably at a temperature between about 150.degree. C. and
250.degree. C. (HCCI mode). When the engine operates in SI mode,
the engine exhaust gas is at stoichiometric conditions with high
temperatures (500 to 600.degree. C.), such that the three-way
catalyst in the lean NO.sub.x trap system of the present invention
effectively converts HC, CO and NO.sub.x.
[0042] It should be noted that in instances where the lean burn
exhaust gas temperature exceeds the operating temperature window of
the first LNT (150 to 300.degree. C.), the second alumina-based
LNT, which is at a lower inlet temperature, can perform the
NO.sub.x reduction under lean conditions.
[0043] It should also be noted that when the engine operation mode
switches from SI mode to median HCCI mode, if the first LNT is
exposed to a temperature higher than its operating temperature
window (above 350.degree. C.), the second alumina-based LNT located
downstream from the three-way catalyst can be active in reducing
NO.sub.x since the second LNT is located at such a distance away
from the first LNT that its inlet temperature is at least
100.degree. C. lower than that of the first LNT.
[0044] A desulphurization (de-SO.sub.x) process may be performed on
the system when the sulfur content on the alumina-based lean
NO.sub.x trap reaches a certain threshold level (HT). This
threshold level is determined by the amount of SO.sub.x storage
materials in the trap, the temperature, the inlet SO.sub.x level,
the exhaust gas flow rate, the operating history of the trap, etc.
The de-SO.sub.x timing may also be determined by a SO.sub.x sensor
(not shown) which may be positioned downstream from the
alumina-based LNT.
[0045] Each time the engine switches from HCCI mode to SI mode
during normal operations (except the rich time during the lean/rich
cycle for lean NO.sub.x trap operation) a de-SO.sub.x process
should be performed unless the sulfur content on the LNT is below a
low threshold value (LT) since the de-SO.sub.x condition is easily
achieved when the engine is in SI mode.
[0046] The alumina-based trap of the present invention has a unique
de-SO.sub.x procedure which is believed to occur because of a weak
interaction between the SO.sub.x and the alumina-based storage
materials. The release of sulfur from the alumina-based trap is
very efficient and provides the advantage of minimum thermal
exposure and fuel penalty during de-SO.sub.x over the use of a
conventional LNT alone.
[0047] During the desulphurization process, exhaust gases in the
alumina-based lean NO.sub.x trap 12 are heated to a temperature of
between about 550.degree. C. and about 650.degree. C. for at least
60 seconds (during SI mode). The resulting de-SO.sub.x product is
comprised mainly of SO.sub.2 (more than 90 wt %), which is a more
favorable sulfur product than the H.sub.2S product typically
achieved with de-SO.sub.x of a conventional LNT.
[0048] In order that the invention may be more readily understood,
reference is made to the following examples which are intended to
illustrate the invention, but not limit the scope thereof.
EXAMPLE 1
[0049] A lean NO.sub.x trap system in accordance with the present
invention comprising an alumina-based LNT and a three-way catalyst
was applied to simulated dual mode HCCI exhaust gases in a
laboratory reactor to verify the efficiencies of the system in
converting the pollutants in various engine operation modes. Table
1 below lists the emission data and exhaust gas temperatures from a
single cylinder dual mode HCCI engine at different engine modes (#1
to #5), and the emission results after the alumina-based LNT and
three way catalyst. TABLE-US-00001 TABLE 1 Data from a single
cylinder HCCI engine and laboratory emission results after
treatment Engine Operation Mode Engine out emission After catalyst
(Lab results) #1 - HCCI AF ratio = 94 T catalyst inlet =
150.degree. C. T engine out = 190.degree. C. NO.sub.x = 0 ppm; HC =
0 ppm NO.sub.x = 3 ppm; HC = 1100 ppm CO = 0.001 ppm CO = 4400 ppm
#2 - HCCI AF ratio = 36 T catalyst inlet = 180.degree. C. T engine
out = 240.degree. C. lean/rich (30/4) NO.sub.x = 140 ppm; HC = 3500
ppm NO.sub.x = 4.04 ppm; HC = 150 ppm CO = 400 ppm CO = 8 ppm #3 -
HCCI AF ratio = 39 T catalyst inlet = 170.degree. C. T engine out =
230.degree. C. lean/rich (60/4) NO.sub.x = 80 ppm; HC = 3800 ppm
NO.sub.x = 1.04 ppm; HC = 180 ppm CO = 400 ppm CO = 9 ppm #4 - SI
AF ratio = 14.7 T catalyst inlet = 500.degree. C. T engine out =
590.degree. C. NO.sub.x = 0 ppm; HC = 18 ppm NO.sub.x = 2000 ppm;
CO = 35 ppm HC = 5000 ppm; CO = 12,500 ppm #5 - SI AF ratio = 14.6
T catalyst inlet = 500.degree. C. T engine out = 600.degree. C.
NO.sub.x = 0 ppm; HC = 32 ppm NO.sub.x = 2000 ppm; CO = 12 ppm HC =
8000 ppm; CO = 9500 ppm
[0050] At engine mode #1--HCCI with relatively low loads, NO.sub.x
concentration was low (3 ppm) and engine out temperature was at
190.degree. C., the catalyst system was running at 150.degree. C.
in lean conditions and effectively removed all the pollutants. At
mode #2--HCCI with median loads, engine exhaust temperature of
about 240.degree. C., and NO.sub.x concentration at about 140 ppm,
a lean/rich cycle of 30 second lean/4 second rich was applied to
the system at about 180.degree. C. The NO.sub.x, HC and CO had high
conversion efficiencies (above 90%). Mode #3--HCCI with a NO.sub.x
concentration of 80 ppm, and a lean/rich cycle of 60/4 was applied
to the LNT system. The pollutants (HC, CO and NO.sub.x) were
converted at high efficiencies (above 90%). Modes #4 and 5--SI with
stoichiometric conditions (air/fuel ratio of about 14.7) at high
temperature (600.degree. C.). The pollutants were converted
efficiently (above 90%) by the three way catalyst without running
the lean/rich cycle.
[0051] It is clear that in the median engine loads when the engine
operates in HCCI mode, the NO.sub.x concentration in the lean
exhaust gas is relatively high such that the lean/rich cycles are
needed for converting the NO.sub.x in the lean exhaust gas, e.g.,
the LNT system functions as a lean NO.sub.x trap. The lean/rich
cycle can be realized by quickly switching the engine from HCCI
mode to SI mode. The ratio of the lean/rich time can be adjusted
with the feedback of in-situ NO.sub.x conversion efficiencies (e.g.
obtained by one or more downstream NO.sub.x sensors) compared with
the engine out NO.sub.x concentration (which is measured either by
a NO.sub.x sensor upstream of the catalyst system or from engine
map) by changing the length of rich time and the frequency (length
of the lean time) to reach the minimum fuel penalty (R-x/y, the
higher, the R, the less the fuel penalty) and maximum NO.sub.x
conversion efficiency (see commonly assigned U.S. application Ser.
No. ______ entitled ALUMINA-BASED LEAN NO.sub.x TRAP SYSTEM AND
METHOD OF USE, the disclosure of which is hereby incorporated by
reference).
[0052] During the low load of HCCI mode (mode #1--HCCI), when the
NO.sub.x concentration is low (e.g., <10 ppm), the lean/rich
cycle is not needed (a NO.sub.x sensor for measuring the engine out
NO.sub.x or engine mapping can provide guidance if lean/rich cycle
is necessary), and the catalyst system of present invention can
effectively convert HC and CO in lean condition (above 150.degree.
C.). When the engine operates at SI mode (modes #4 and 5--SI),
these is also no need of modification of the air fuel ratio (or
lean/rich cycle). Since the exhaust gas is at stoichiometric
(air/fuel ratio about 14.7) and high temperature (500 to
600.degree. C.), the three way catalyst can effectively remove the
pollutants (HC, CO and NO.sub.x).
[0053] FIG. 4 illustrates the de-SOx process of the LNT system of
the present invention (with sulfur loading of 1.14 gram/liter)
under the unique de-SOx method of the alumina-based LNT. It is
clear that sulfur can be removed (out of the system) very
efficiently (in about 60 seconds) at 550 to 650.degree. C. under
slightly rich condition without being captured by the downstream
three way catalyst.
[0054] While certain representative embodiments and details have
been shown for purposes of illustrating the invention, it will be
apparent to those skilled in the art that various changes in the
methods and apparatus disclosed herein may be made without
departing from the scope of the invention, which is defined in the
appended claims.
* * * * *