U.S. patent application number 13/526926 was filed with the patent office on 2013-11-28 for systems and methods to mitigate nox and hc emissions at low exhaust temperatures.
The applicant listed for this patent is Cary Henry, Michael J. Ruth. Invention is credited to Cary Henry, Michael J. Ruth.
Application Number | 20130312392 13/526926 |
Document ID | / |
Family ID | 49620494 |
Filed Date | 2013-11-28 |
United States Patent
Application |
20130312392 |
Kind Code |
A1 |
Henry; Cary ; et
al. |
November 28, 2013 |
SYSTEMS AND METHODS TO MITIGATE NOX AND HC EMISSIONS AT LOW EXHAUST
TEMPERATURES
Abstract
Systems and methods are provided for managing low temperature
NO.sub.x and HC emissions, such as during a cold start of an
internal combustion engine. The systems and methods include storing
NO.sub.x and HC emissions at low temperatures and passively
releasing these emissions as the temperature of the exhaust system
increases.
Inventors: |
Henry; Cary; (Columbus,
IN) ; Ruth; Michael J.; (Franklin, IN) |
|
Applicant: |
Name |
City |
State |
Country |
Type |
Henry; Cary
Ruth; Michael J. |
Columbus
Franklin |
IN
IN |
US
US |
|
|
Family ID: |
49620494 |
Appl. No.: |
13/526926 |
Filed: |
June 19, 2012 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
61650722 |
May 23, 2012 |
|
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|
Current U.S.
Class: |
60/274 ;
60/287 |
Current CPC
Class: |
F01N 3/103 20130101;
F01N 2610/02 20130101; F01N 3/0835 20130101; F01N 3/0842 20130101;
Y02T 10/24 20130101; F01N 3/208 20130101; Y02T 10/12 20130101 |
Class at
Publication: |
60/274 ;
60/287 |
International
Class: |
F01N 3/24 20060101
F01N003/24; F01N 3/20 20060101 F01N003/20 |
Claims
1. A method, comprising: storing in an exhaust flowpath, upstream
of a NO.sub.x reduction catalyst, hydrocarbon (HC) and oxides of
nitrogen (NO.sub.x) emissions from an internal combustion engine
during low exhaust temperature operation; releasing the stored HC
and NO.sub.x emissions into the exhaust flowpath as the exhaust
temperature increases toward an effective operating temperature;
and treating the released HC and NO.sub.x emissions with an
oxidation catalyst and the NO.sub.x reduction catalyst.
2. The method of claim 1, wherein the NO.sub.x reduction catalyst
is a selective catalytic reduction catalyst.
3. The method of claim 1, wherein the oxidation catalyst is a
hydrocarbon storage device catalyst and storing HC emissions
includes storing HC emissions on the surface of the hydrocarbon
storage device catalyst.
4. The method of claim 3, further comprising oxidizing the stored
HC with the hydrocarbon storage device catalyst.
5. The method of claim 1, wherein storing NO.sub.x emissions
includes storing NO.sub.x emissions on the surface of a NO.sub.x
storage device catalyst.
6. The method of claim 5, wherein the NO.sub.x storage device is a
NO.sub.x adsorber.
7. The method of claim 1, wherein the effective operating
temperature is around 200.degree. Celsius.
8. The method of claim 1, further comprising delaying reductant
dosing during the low exhaust temperature operation so that a
reductant amount dosed into the exhaust flowpath during low exhaust
temperature operation is insufficient for the NO.sub.x reduction
catalyst to treat the NO.sub.x emissions from the internal
combustion engine.
9. A method, comprising: operating an internal combustion engine to
produce hydrocarbon (HC) and oxides of Nitrogen (NO.sub.x)
emissions into an exhaust flowpath during low exhaust temperature
operation; storing, upstream of a NO.sub.x reduction catalyst, HC
and NO.sub.x emissions from the internal combustion engine during
low exhaust temperature operation; and providing a reductant dosing
command that treats the NO.sub.x emissions with the NO.sub.x
reduction catalyst when the exhaust temperature reaches an
effective operating temperature that releases the stored HC and
NO.sub.x emissions.
10. The method of claim 9, further comprising delaying reductant
dosing during the low exhaust temperature operation so that a
reductant amount dosed into the exhaust flowpath during low exhaust
temperature operation is insufficient for a NO.sub.x reduction
catalyst to treat the NO.sub.x emissions from the internal
combustion engine.
11. The method of claim 9, wherein storing HC emissions includes
storing HC emissions on the surface of a hydrocarbon storage device
catalyst and wherein releasing the stored HC emissions includes
oxidizing the HC as the exhaust temperature increases toward the
effective operating temperature.
12. The method of claim 11, wherein storing NO.sub.x emissions
includes storing NO.sub.x emissions on the surface of a NO.sub.x
storage device catalyst.
13. The method of claim 12, wherein the NO.sub.x storage device is
a NO.sub.x adsorber.
14. The method of claim 9, wherein the effective operating
temperature is around 200.degree. Celsius.
15. The method of claim 9, wherein the NO.sub.x reduction catalyst
is a selective catalytic reduction catalyst.
16. A system, comprising: an internal combustion engine; an exhaust
conduit fluidly coupled to the internal combustion engine; a
hydrocarbon storage device fluidly coupled to the exhaust conduit;
a NO.sub.x adsorber fluidly coupled to the exhaust conduit; a
NO.sub.x reduction catalyst downstream of the NO.sub.x adsorber;
and a reductant doser operationally coupled to the exhaust conduit
upstream of the NO.sub.x reduction catalyst and downstream of the
NO.sub.x adsorber.
17. The system of claim 16, wherein the NO.sub.x reduction catalyst
is downstream of the hydrocarbon storage device.
18. The system of claim 17, wherein the reductant doser is
operationally coupled to the exhaust conduit downstream of the
hydrocarbon storage device and the NO.sub.x adsorber.
19. The system of claim 16, wherein the reductant doser is
operationally coupled to the exhaust conduit downstream of the
hydrocarbon storage device and the NO.sub.x adsorber.
20. The system of claim 16, further comprising a controller,
comprising: a NO.sub.x ratio determination module structured to
determine an NO.sub.x amount at an outlet of the NO.sub.x reduction
catalyst; a temperature determination module structured to
determine a present operating temperature of the exhaust gas in the
exhaust flowpath; a dosing control module structured to determine a
reductant doser command in response to the NO.sub.x amount to
achieve a desired NO.sub.x emissions from the NO.sub.x reduction
catalyst.
21. The system of claim 20, wherein the controller is configured to
provide a delayed reductant doser command during low exhaust
temperature operating conditions
22. The system of claim 16, wherein the hydrocarbon storage device
includes a catalyst configured to store hydrocarbon (HC) emissions
thereon during low exhaust temperature operating conditions and to
oxidize the stored HC when the exhaust temperature reaches an
effective temperature.
23. The system of claim 22, wherein the NO.sub.x adsorber is
structured to adsorb NO.sub.x emissions during low exhaust
temperature operating conditions and release and oxidize NO.sub.x
emissions when the exhaust temperature reached an effective
temperature for NO.sub.x conversion over the NO.sub.x reduction
device.
24. The system of claim 16, further comprising a first NO.sub.x
sensor at an inlet of the hydrocarbon storage device and a second
NO.sub.x sensor at an outlet of the NO.sub.x reduction
catalyst.
25. The system of claim 16, further comprising a NO.sub.x sensor
between the NO.sub.x adsorber and the NO.sub.x reduction
catalyst.
26. The system of claim 16, further comprising a NO.sub.x sensor
upstream of the NO.sub.x reduction catalyst.
Description
CROSS-REFERENCE TO RELATED APPLICATIONS
[0001] The present application claims the benefit of the filing
date of Provisional Application No. 61/650,722 filed on May 23,
2012, which is incorporated herein by reference.
BACKGROUND
[0002] Control of selective catalytic reduction (SCR) catalysts is
of increasing interest to meet modern internal combustion engine
emissions standards. The effectiveness of a typical SCR catalyst in
removing oxides of nitrogen (NO.sub.x) emissions is sensitive to
the temperature of the exhaust gas at the inlet to the SCR
catalyst. Copper exchanged zeolite based SCR catalysts are
formulated to operate satisfactorily over a fairly wide temperature
range. However, current state of the art Cu-Zeolite formulations
operate at peak efficiency when subjected to exhaust gas
temperatures of 200-400.degree. C. For certification of certain
diesel engines, the emissions performance of the engine during the
cold portion of the certification cycle is weighted almost equally
with the emissions performance of the engine during the hot portion
of the certification cycle. For this reason, improvements in
preventing hydrocarbon (HC) and NO.sub.x emissions produced by the
engine from slipping through the aftertreatment system at low
temperature exhaust conditions, such as at temperatures less than
200.degree. C., are desired.
[0003] Typical diesel A/T systems include a diesel oxidation
catalyst (DOC) and a diesel particulate filter (DPF) in addition to
the SCR. The DOC is responsible for oxidation of hydrocarbons (HC),
carbon monoxide (CO), and nitric oxide (NO). Similar to the SCR
catalyst, the DOC is not able to effectively and efficiently
oxidize these molecules at cold exhaust temperatures. In order to
meet NO.sub.x and HC emissions levels (for example, 0.02 and 0.01
g/mile, respectively for Tier 2 Bin 2 federal certification) at low
temperature conditions, improvements in aftertreatment designs are
required to mitigate the slip of these criteria pollutants through
the exhaust flowpath during low temperature operation. Accordingly,
further technological developments in this area are desirable.
SUMMARY
[0004] One embodiment is a unique method and system for managing
low temperature NO.sub.x and HC emissions to improve the NO.sub.x
conversion efficiency of diesel aftertreatment systems under low
exhaust temperature conditions. In one embodiment, there is
provided a multiple component aftertreatment system that includes
passively operated HC and NO.sub.x storage devices for improved low
temperature mitigation of NO.sub.x and HC emissions to achieve
desired emissions levels for light duty vehicles, although
applications with other vehicles are not precluded. The systems and
methods reduce the need for external devices intended to
artificially increase the exhaust gas temperature for cold start
cycles, which is beneficial since such external devices tend to
increase fuel consumption and greenhouse gas emissions, although
the use of such external devices are not precluded. The systems and
methods disclosed herein provide reductions in cost and fuel
consumption over current thermal management strategies to mitigate
low temperature NO.sub.x and HC emissions. Further embodiments,
forms, objects, features, advantages, aspects, and benefits shall
become apparent from the following description and drawings.
BRIEF DESCRIPTION OF THE DRAWINGS
[0005] FIG. 1 is an exemplary system for reducing emissions of HC
and NO.sub.x of an internal combustion engine during low exhaust
temperature operating conditions.
[0006] FIG. 2 is a schematic of a controller comprising a portion
of the system of FIG. 1.
[0007] FIG. 3 is a graph showing an estimated impact of a
hydrocarbon storage device on HC slip flow over time during low
temperature exhaust operating conditions.
DESCRIPTION OF THE ILLUSTRATIVE EMBODIMENTS
[0008] For the purposes of promoting an understanding of the
principles of the invention, reference will now be made to the
embodiments illustrated in the drawings and specific language will
be used to describe the same. It will nevertheless be understood
that no limitation of the scope of the invention is thereby
intended, any alterations and further modifications in the
illustrated embodiments, and any further applications of the
principles of the invention as illustrated therein as would
normally occur to one skilled in the art to which the invention
relates are contemplated herein.
[0009] There is disclosed systems and methods for reduction in HC
and NO.sub.x emissions at low exhaust temperature operating
conditions for an internal combustion engine. The systems and
methods reduce criteria pollutants at least during low exhaust
temperature conditions. The disclosed systems and methods are
configured so that the vehicles equipped therewith are operable to
meet emissions standards during low exhaust temperature operating
conditions without the need for external aftertreatment heating
systems, which increase fuel consumption and greenhouse gas
emissions from the vehicle, although the use of such external
systems is not precluded. In one embodiment, the systems and
methods have application for light duty certified chassis vehicles,
although applications with other vehicle types are not
precluded.
[0010] The systems and methods include an aftertreatment system
architecture configured to temporarily store HC emissions and
NO.sub.x emissions during periods of low exhaust temperature
operation, and then passively release the stored NO.sub.x and HC
emissions for aftertreatment as the exhaust temperature increases.
The systems and methods are configured so that at temperatures
where HC and NOx emissions are released, the diesel oxidation
catalyst (DOC) and SCR catalysts are effective at mitigating the
released HC and NO.sub.x emissions from the storage devices before
exiting the tailpipe.
[0011] In one embodiment, the aftertreatment system includes a
close coupled HC storage device (HCSD) located directly downstream
of the turbocharger, with a close coupled NO.sub.x storage device
(NSD) located directly downstream of the HCSD. At low exhaust
temperatures, the HCSD readily adsorbs and stores HC. In one
specific embodiment, the HCSD includes a catalyst, such as a
zeolite-based catalyst, for storing and adsorbing HC. As the
exhaust temperature increases, the HCSD effectively oxidizes HC in
the gas phase that are stored on the surface of the HCSD to form
H.sub.2O and CO.sub.2. The NSD is any suitable component, such as a
NO.sub.x adsorber, capable of passively storing NO.sub.x at low
exhaust temperature, and then releasing the stored NO.sub.x as the
exhaust temperature increases. The NSD may also have an oxidation
function, primarily for NO oxidation to NO.sub.2, but under normal
operating conditions is not capable of effectively reducing
NO.sub.x to N.sub.2 and H.sub.2O. The NSD relies on a downstream
selective catalytic reduction (SCR) catalyst or other NO.sub.x
reduction catalyst to chemically reduce the NO.sub.x to N.sub.2 and
H.sub.2O.
[0012] In a further embodiment, systems and methods for reducing
the emission of HC and NO.sub.x from lean burn internal combustion
engines for low exhaust temperature operating conditions are
disclosed. As shown in FIG. 1, an exemplary aftertreatment system
10 includes a close coupled HCSD 12 and NSD 14 followed by a
standard SCR or NAC-type NO.sub.x reduction catalyst 16 to receive
exhaust gas produced by an internal combustion engine 20 into
exhaust flowpath 18. The HCSD 12 and NSD 14 are passively operated
devices, which require little or no active control strategies,
although the use of active control strategies is not precluded.
[0013] At low exhaust gas temperatures which result in low catalyst
temperatures, the HCSD 12 readily adsorbs and stores HC on the
surface of a catalyst until the HCSD 12 reaches a surface
temperature where it can effectively oxidize the stored HC to form
CO.sub.2 and H.sub.2O. The NSD 14 readily adsorbs and stores
NO.sub.x on the surface of its catalyst under low exhaust
temperature conditions, and then begins to desorb this NO as the
exhaust temperature and therefore the NSD catalyst temperature
increases. The NSD 14 is configured to release the stored NO.sub.x
at an exhaust temperature where the reduction catalyst 16 is highly
effective for reducing NO.sub.x to N.sub.2 and H.sub.2O. Once the
aftertreatment system 10 reaches operating temperature, either or
both of the catalysts of the HCSD 12 and the NSD 14 may operate as
DOC catalysts, and together are responsible for the oxidation of
HC, CO and NO.
[0014] System 10 may include a controller 100 and other
aftertreatment components in addition to those shown in FIG. 1. For
example, system 10 typically includes a reductant doser 17
operationally coupled to the exhaust conduit at a position upstream
of the reduction catalyst 16. The reductant injected into exhaust
flowpath 18 is any type of reductant utilized in a NO.sub.x
reduction system. For example, the reductant can include at least
ammonia (gaseous or aqueous) and urea. System 10 may also include a
diesel particulate filter (DPF) forming, with the HCSD 12 and NSD
14, a DOC/DPF system positioned upstream of reduction catalyst 16
during engine operation where exhaust temperatures are effective
for NO.sub.x reduction with reduction catalyst 16. The system 10
may include an ammonia oxidation catalyst (AMOX) downstream of the
reduction catalyst 16. In certain embodiments, the AMOX may not be
present, or the AMOX may be commingled with the reduction catalyst
16 (or the last SCR catalyst, where multiple SCR catalysts are
present), for example with a washcoat applied toward the rear
portion of the reduction catalyst 16 that is responsive to at least
partially oxidize ammonia. In other embodiments, any of these
components may be present or missing, catalyzed or not catalyzed,
and may be arranged in alternate order. Further, certain components
or all components may be provided in the same or separate
housings.
[0015] For system 10 including controller 100, controller 100 can
include a number of modules structured to functionally execute
operations for controlling the SCR system. In certain embodiments,
the controller forms a portion of a processing subsystem including
one or more computing devices having memory, processing, and
communication hardware. The controller 100 may be a single device
or a distributed device, and the functions of the controller may be
performed by hardware or software. The controller 100 may be in
communication with any sensor, actuator, datalink, and/or network
in the system.
[0016] In certain embodiments, such as shown in FIG. 2, the
controller 100 includes a NO.sub.x determination module 102, a
temperature determination module 104, and a dosing control module
106. The description herein including modules emphasizes the
structural independence of the aspects of the controller 100, and
illustrates one grouping of operations and responsibilities of the
controller 100. Other groupings that execute similar overall
operations are understood within the scope of the present
application. Modules may be implemented in hardware and/or software
on computer readable medium, and modules may be distributed across
various hardware or software components. More specific descriptions
of certain embodiments of controller operations are included in the
section referencing FIG. 2.
[0017] The exemplary system 10 further includes various sensors.
The illustrated sensors in FIG. 1 include a first NO.sub.x sensor
22 positioned upstream of the HCSD 12 and a second NO.sub.x sensor
24 positioned downstream of the reduction catalyst 16.
Alternatively or additionally, a NO.sub.x sensor 38 can be provided
at the outlet of NSD 14, or between the inlet to reduction catalyst
16 and the outlet of NSD 14. System 10 also includes a first
temperature sensor 26 at the inlet of HCSD 12, a second temperature
28 between HCSD 12 and NSD 14, a third temperature sensor 30 at the
outlet of NSD 14, and a fourth temperature sensor 32 at the outlet
of reduction catalyst 16. Other sensors can be provided to measure
or determine the mass flow through the exhaust system, the
temperature of any component of the aftertreatment system, the
amount of ammonia stored in reduction catalyst 16 or outlet
therefrom, etc.
[0018] The illustrated sensors are exemplary only, and may be
re-positioned, removed, substituted, and other sensors may be
present that are not illustrated in FIG. 1. Further, certain
sensors may instead be virtual sensors that are calculated from
other parameters available to the system 10, or values that would
be indicated by sensors may instead be supplied to a computer
readable memory location, via a datalink or network communication,
or otherwise be made available to the system 10 where the sensor
providing the sensed parameter is not a part of the defined system
10.
[0019] The exemplary controller 100 in FIGS. 1-2 is configured for
executing operations to provide a reductant doser command for the
effective removal of NO.sub.x emissions with reduction catalyst 16.
The controller operations of the controller 100 in FIG. 2 include
operations that adjust nominal control operations for a NO.sub.x
aftertreatment system utilizing a reductant. Nominal control
operations for a NO.sub.x aftertreatment system, including an SCR
aftertreatment system, are understood in the art and are not
described further herein. Any nominal NO.sub.x aftertreatment
control operations may be utilized by system 10 disclosed
herein.
[0020] The controller 100 includes a NO.sub.x determination module
102 that receives NO.sub.x parameters 108 from NO.sub.x sensors 22,
24, 38 and determines an amount of NO.sub.x emitted from engine 20
and from reduction catalyst 16, respectively. Controller 100 can
also be configured to determine or calculate and amount of NO.sub.x
at the outlet of NSD 14. Controller 100 also includes a temperature
determination module 104 that receives temperature signals from
temperature sensors 26, 28, 30, 32 to determine a temperature of
the exhaust gas in flowpath 18 and/or of the various catalysts of
the aftertreatment components in flowpath 18. Controller 100
further includes a dosing control module 106 that determines an
appropriate dosing command for reductant to be injected in flowpath
18 to provide a desired emissions level for NO.sub.x at the outlet
of reduction catalyst 16 and ultimately to the tailpipe.
[0021] During low temperature operating conditions for engine 20
and for exhaust gas and/or aftertreatment components in flowpath
18, reduction catalyst 16 is ineffective in treating emissions of
NO.sub.x to meet desired emissions level targets. Furthermore,
traditional oxidation catalysts upstream of reduction catalyst 16
are ineffective in removing HC to meet criteria emissions levels at
low temperature operating conditions. Therefore, HCSD 12 is
configured to store HC, and NSD 14 is configured to store NO.sub.x
during low exhaust temperature operating conditions until the
aftertreatment components of system 10 are raised to a temperature
effective to remove the criteria pollutants from the emissions of
engine 20.
[0022] The amount of accumulation during low exhaust temperature
operating conditions of NO.sub.x in NSD 14 can be determined by the
difference between the amount of NO.sub.x detected by upstream
NO.sub.x sensor 22 and the corresponding amount detected by
downstream NO.sub.x sensor 24 and converted by oxidation catalyst
16 during low temperature operation. Dosing control module 106 is
configured to determine a dosing command that delays reductant
dosing during low temperature operating conditions since NO.sub.x
sensor 24 senses NO.sub.x levels that are reduced or lower than the
levels determined by NO.sub.x sensor 22 due to the NO.sub.x storage
at NSD 14. As the exhaust gas temperature increases to and above an
effective temperature, dosing control module 106 is configured to
increase reductant dosing to treat the NO.sub.x emissions released
from NSD 14 as determined by one or both of NO.sub.x sensor 38 and
NO.sub.x sensor 24, or by a calculated or sensed NO.sub.x amount at
the outlet of NSD 14. Furthermore, in certain embodiments, dosing
control module 106 can be configured to anticipate a future
NO.sub.x emissions load and timing of the release of the stored
NO.sub.x emissions by monitoring temperature parameters 110. The
amount of reductant dosing can be increased prior to release of
NO.sub.x emissions to provide a sufficient amount of reductant on
reduction catalyst 16 to meet the expected increased in NO.sub.x
emissions.
[0023] The dosing control module 106 provides a reductant doser
command 114 to reductant doser 17 in response to a threshold
deviation value 116. The threshold deviation value 116 includes a
determination that NO.sub.x emissions at NO.sub.x sensor 24 is
approaching or meeting a threshold deviation from an emissions
level target value which requires reductant to be supplied to
reduction catalyst 16. The reductant doser command 114 provided by
the dosing control module 106 may include a reductant amount to be
supplied to reduction catalyst 16. The dosing control module 106
provides the reductant doser command 114 in response to the
threshold deviation value 116 indicating that the present NO.sub.x
emissions level deviates more than a threshold amount from a
NO.sub.x emissions level target. The reductant doser command 114
may be provided under any control scheme understood in the art,
and/or under specific control schemes described herein. The
reductant doser command 114 may include an actuator command value,
a voltage or other electrical signal, and/or a datalink or network
command. In certain embodiments, a reductant doser in a system
including the controller 100 is responsive to the reductant doser
command 114 to provide reductant to an exhaust stream at the
position of the reductant doser 17 upstream of the reduction
catalyst 16.
[0024] Dosing control module 106 can further be configured to
provide a reductant doser command 114 that can be delayed to
account for the amount of NO.sub.x stored by NSD 14 during low
temperature exhaust conditions. As used herein, a delayed reductant
doser command includes decreasing the rate at which reductant is
injected and/or decreasing the range of engine operating conditions
in which reduction catalyst 16 is utilized for treatment of
NO.sub.x emissions, including those conditions which otherwise
would have resulted in treatment of emissions of NOx from engine 20
by supplying reductant to reduction catalyst 16 without NO.sub.x
storage by NSD 14 upstream of reduction catalyst 16. However,
injection of reductant for storage on reduction catalyst 16 during
low temperature operation is not precluded.
[0025] The descriptions here provide illustrative embodiments of
performing procedures for controlling an aftertreatment system for
low temperature operating conditions. Operations illustrated are
understood to be exemplary only, and operations may be combined or
divided, and added or removed, as well as re-ordered in whole or
part, unless stated explicitly to the contrary herein. Certain
operations illustrated may be implemented by a computer executing a
computer program product on a computer readable medium, where the
computer program product comprises instructions causing the
computer to execute one or more of the operations, or to issue
commands to other devices to execute one or more of the
operations.
[0026] An exemplary HCSD 12 is operable to store HC over a range of
operating temperatures below an effective operating temperature.
For example, at temperatures below 200.degree. C., HCSD 12 is
effective at storing HC emissions typically seen in operation of a
diesel engine. As the exhaust temperatures approach and exceed
200.degree. C., the lightoff of the HC emissions stored in HCSD 12
is effective to oxidize the HC to form CO.sub.2 and H.sub.2O. In
one embodiment, the catalyst of HCSD 12 is a zeolite catalyst with
an oxidation catalyst thereon.
[0027] As shown in graph 300 of FIG. 3, line 302 indicates the
cumulative HC received at the inlet to HCSD 12 over time at the
start of a low temperature operating condition. Lines 304, 306
indicate the minimal outlet of HC from HCSD 12 over time during the
low temperature operating condition. As the operating temperature
increases over time, as indicated by line 308, the stored HC stored
until a sufficiently high catalyst temperature for HCSD 12 is
attained to oxidize HC.
[0028] As is evident from the figures and text presented above, a
variety of embodiments according to the present invention are
contemplated.
[0029] An exemplary set of embodiments is a method including
storing in an exhaust flowpath, upstream of a NO.sub.x reduction
catalyst, hydrocarbon and NO.sub.x emissions from an internal
combustion engine during low exhaust temperature operation;
releasing the stored hydrocarbons and NO.sub.x emissions into the
exhaust flowpath as the exhaust temperature increases toward an
effective operating temperature; and treating the released
hydrocarbons and NO.sub.x emissions with the NO.sub.x reduction
catalyst.
[0030] In certain embodiments of the method, the NO.sub.x reduction
catalyst is a selective catalytic reduction catalyst. In other
embodiments, the method includes storing hydrocarbon emissions on
the surface of a hydrocarbon storage device catalyst. In other
embodiments, the method includes storing NO.sub.x emissions
includes storing NO.sub.x emissions on the surface of a NO.sub.x
storage device catalyst. In other embodiments, the NO.sub.x storage
device is a NO.sub.x adsorber. In certain embodiments, the
effective operating temperature is around 200.degree. Celsius. In
other embodiments, the method further includes delaying reductant
dosing during the low exhaust temperature operation so that a
reductant amount dosed into the exhaust flowpath during low exhaust
temperature operation is insufficient for the NO.sub.x reduction
catalyst to treat the NO.sub.x emissions from the internal
combustion engine.
[0031] Another set of exemplary embodiments is a method comprising:
operating an internal combustion engine to produce hydrocarbon and
NO.sub.x emissions into an exhaust flowpath during low exhaust
temperature operation; storing, upstream of a NO.sub.x reduction
catalyst, HC and NO.sub.x emissions from the internal combustion
engine during low exhaust temperature operation; and providing a
reductant dosing command that treats the NO.sub.x emissions with
the NO.sub.x reduction catalyst when the exhaust temperature
reaches an effective operating temperature that releases the stored
HC and NO.sub.x emissions.
[0032] In yet other embodiments, the method further comprises
delaying reductant dosing during the low exhaust temperature
operation so that a reductant amount dosed into the exhaust
flowpath during low exhaust temperature operation is insufficient
for a NO.sub.x reduction catalyst to treat the NO.sub.x emissions
from the internal combustion engine. In another embodiment, storing
hydrocarbon emissions includes storing hydrocarbon emissions on the
surface of a hydrocarbon storage device catalyst and releasing the
stored hydrocarbons includes oxidizing the hydrocarbons as the
exhaust temperature increases toward the effective operating
temperature. In one refinement of this embodiment, storing NO.sub.x
emissions includes storing NO.sub.x emissions on the surface of a
NO.sub.x storage device catalyst. In yet another refinement, the
NO.sub.x storage device is a NO.sub.x adsorber. In additional
embodiments, the effective operating temperature is around
200.degree. Celsius. In other embodiments, the NO.sub.x reduction
catalyst is a selective catalytic reduction catalyst.
[0033] Another exemplary set of embodiments is a system including
an internal combustion engine; an exhaust conduit fluidly coupled
to the internal combustion engine; a hydrocarbon storage device
fluidly coupled to the exhaust conduit; a NO.sub.x adsorber fluidly
coupled to the exhaust conduit; a NO.sub.x reduction catalyst
downstream of the NO.sub.x adsorber; and a reductant doser
operationally coupled to the exhaust conduit upstream of the
NO.sub.x reduction catalyst and downstream of the NO.sub.x
adsorber.
[0034] In certain embodiments, the system includes the NO.sub.x
reduction catalyst downstream of the hydrocarbon storage device. In
one refinement of this embodiment, the reductant doser is
operationally coupled to the exhaust conduit downstream of the
hydrocarbon storage device and the NO.sub.x adsorber. In another
embodiment, the reductant doser is operationally coupled to the
exhaust conduit downstream of the hydrocarbon storage device and
the NO.sub.x adsorber.
[0035] In certain embodiments, the system includes a controller
comprising a NO.sub.x ratio determination module structured to
determine a NO.sub.x amount at an outlet of the NO.sub.x reduction
catalyst; a temperature determination module structured to
determine a present operating temperature of the exhaust gas in the
exhaust flowpath; and a dosing control module structured to
determine a reductant doser command in response to the NO.sub.x
amount to achieve a desired NO.sub.x emissions from the NO.sub.x
reduction catalyst.
[0036] In another exemplary embodiment of the system, the
controller is configured to provide a delayed reductant doser
command during low exhaust temperature operating conditions. In
another embodiment, the hydrocarbon storage device includes a
catalyst configured to store hydrocarbon emissions thereon during
low exhaust temperature operating conditions and to oxidize the
stored hydrocarbons when the exhaust temperature reaches an
effective temperature. In a refinement of this embodiment, the
NO.sub.x adsorber is structured to adsorb NO.sub.x emissions during
low exhaust temperature operating conditions and release and
oxidize NO.sub.x emissions when the exhaust temperature reached an
effective temperature. In another embodiment, the system includes a
first NO.sub.x sensor at an inlet of the hydrocarbon storage device
and a second NO.sub.x sensor at an outlet of the nitrous oxide
reduction catalyst. In another embodiment, the system includes a
NO.sub.x sensor at an outlet of the NO.sub.x storage device.
[0037] While the invention has been illustrated and described in
detail in the drawings and foregoing description, the same is to be
considered as illustrative and not restrictive in character, it
being understood that only certain exemplary embodiments have been
shown and described and that all changes and modifications that
come within the spirit of the inventions are desired to be
protected. In reading the claims, it is intended that when words
such as "a," "an," "at least one," or "at least one portion" are
used there is no intention to limit the claim to only one item
unless specifically stated to the contrary in the claim. When the
language "at least a portion" and/or "a portion" is used the item
can include a portion and/or the entire item unless specifically
stated to the contrary.
* * * * *