Title of Invention

AN IMPROVED NITROGEN OXIDES (NOX) REDUCTION SYSTEM AND METHOD FOR AN INTERNAL COMBUSTION ENGINE

Abstract An exhaust after-treatment system for an internal combustion engine includes a lean NOx catalyst having an exhaust stream from the internal combustion engine flowing therethrough. A NOx absorber catalyst is downstream of the lean NOx catalyst. The NOx absorber is selectively regenerated to increase a NOx reduction efficiency of the exhaust after- treatment system.
Full Text 1
GP-307394-PTE-CD
OPTIMIZED NOx REDUCTION SYSTEM
FIELD OF THE INVENTION
[0001] The present invention relates to internal combustion engines,
and more particularly to an optimized NOx reduction exhaust system.
BACKGROUND OF THE INVENTION
[0002] Internal combustion engines generate drive torque by
combusting an air and fuel mixture within cylinders. Exhaust that is generated
via the combustion process is exhausted from the cylinders and is treated in
an after-treatment system. During the combustion process, fuel is oxidized
and hydrogen (H) and carbon (C) combine with air. Various chemical
compounds are formed including carbon dioxide (CO2), water (H2O), carbon
monoxide (CO), nitrogen oxides (NOx), unburned hydrocarbons (HC), sulfur
oxides (SOx), and other compounds.
[0003] The after-treatment systems traditionally include a catalytic
converter that reduces exhaust emissions by chemically converting the
exhaust gas into carbon dioxide (CO2), nitrogen (N), and water (H2O). In
some cases, a lean NOx catalyst is implemented. Lean NOx technology, also
known as HC selective catalytic reduction (SCR) has various formulations
(e.g., platinum/alumina, copper and substituted zeolite. Platinum on alumina
(Pt/AI2O3) functions at low temperatures, has higher peak conversion of
approximately 40% at 225°C, but has a very narrow temperature window of
operation (e.g., between 180 - 280°C). As a result, this formulation is not very
useful by itself. Another disadvantage of platinum catalysts has been their
SOx oxidation activity and it's susceptibility to deactivation by sulfur.
[0004] NOx absorbers have also been developed based on acid-
base wash-coat chemistry. The NOX is absorbed and is stored in the NOx
absorber catalyst wash-coat during lean operating conditions (i.e., higher than
stoichiometric air to fuel ratio). The NOx is released and is catalytically
converted to nitrogen during rich operating conditions (i.e., lower than

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stoichiometric air to fuel ratio). Barium-based NOx absorbers have high
conversion efficiency but are only active at increased temperatures (e.g.,
greater than approximately 250°C). Also, NOx absorbers require periodic
desulfation.
SUMMARY OF THE INVENTION
[0005] Accordingly, the present invention provides an exhaust after-
treatment system that overcomes the deficiencies of the above-described
after-treatment technologies. The exhaust after-treatment system includes a
lean NOx catalyst having an exhaust stream from said internal combustion
engine flowing therethrough. A NOx absorber catalyst is downstream of the
lean NOx catalyst. The NOx absorber is selectively regenerated to increase
the NOx reduction efficiency of the exhaust after-treatment system.
[0006] In another feature, the NOx absorber catalyst is regenerated
when the NOx reduction demand is greater than a high threshold.
[0007] In another feature, the lean NOx catalyst alone reduces a
NOx content of the exhaust stream when a NOx reduction demand is less
than a low threshold.
[0008] In still other features, hydrocarbon (HC) is introduced into the
exhaust stream when a NOx reduction demand is greater than a first
threshold and is less than a second threshold. The HC is introduced via at
least one of spark advance, post-combustion in-cylinder fuel injection and in-
exhaust injection downstream of the internal combustion engine.
[0009] In yet another feature, the exhaust after-treatment system
further includes a hydrocarbon (HC) dosing unit disposed upstream of one of
the lean NOx catalyst and the NOx absorber catalyst.
[0010] Further areas of applicability of the present invention will
become apparent from the detailed description provided hereinafter. It should
be understood that the detailed description and specific examples, while
indicating the preferred embodiment of the invention, are intended for
purposes of illustration only and are not intended to limit the scope of the
invention.

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BRIEF DESCRIPTION OF THE DRAWINGS
[0011] The present invention will become more fully understood
from the detailed description and the accompanying drawings, wherein:
[0012] Figure 1 is a functional block diagram of an engine system
including an optimized NOx reduction exhaust system in accordance with the
present invention; and
[0013] Figure 2 is a flowchart illustrating exemplary steps executed
using an optimized NOx reduction control of the present invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[0014] The following description of the preferred embodiment is
merely exemplary in nature and is in no way intended to limit the invention, its
application, or uses. For purposes of clarity, the same reference numbers will
be used in the drawings to identify similar elements. As used herein, the term
module refers to an application specific integrated circuit (ASIC), an electronic
circuit, a processor (shared, dedicated, or group) and memory that execute
one or more software or firmware programs, a combinational logic circuit,
and/or other suitable components that provide the described functionality.
[0015] Referring now to Figure 1, an engine system 10 includes an
internal combustion engine 12 and an optimized NOx exhaust system 14 in
accordance with the present invention. The engine 12 generates drive torque
that is used to propel a vehicle, within which the engine system 10 is
implemented, and/or drive accessory loads including, but not limited to, an
alternator and a fluid pump (not shown). Air is drawn into an intake manifold
16 through a throttle 18. The air is distributed to cylinders (not shown) of the
engine 12 and is mixed with fuel to form a combustion mixture. The
combustion mixture is ignited within the cylinder to reciprocally drive a piston
(not shown). The combustion processes generates exhaust gas that exits the
engine 12 through an exhaust manifold 20 and that is treated in the optimized
NOx exhaust system 14.
[0016] A control module 22 regulates operation of the engine
system 10 based on various engine system operating conditions. A manifold
absolute pressure (MAP) sensor 24 is responsive to the vacuum pressure

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within the intake manifold 16 and generates a MAP signal based thereon. An
engine RPM sensor 26 is responsive to an engine RPM and generates a
signal based thereon. An exhaust temperature sensor 28 is disposed
downstream of the exhaust manifold 20 and is responsive to the exhaust
temperature (TEXH) and generates a signal based thereon.
[0017] The optimized NOx exhaust system 14 includes a lean NOx
catalyst 30 disposed upstream of a NOx absorber catalyst 32. An HC dosing
unit 34 is disposed upstream of the lean NOx catalyst 30. The HC dosing unit
34 selectively injects HCs into the exhaust stream, which is used for lean NOx
catalyst 30 and NOx absorber catalyst 32 regeneration and desulfation. It is
also anticipated that post-combustion fuel injection can be implemented to
increase the HC content of the exhaust stream, whereby fuel is injected into
the cylinder to be exhausted from the cylinder with the exhaust. Further,
advanced combustion (i.e., HCCI) includes relatively higher engine out HC
levels. This increased HC level is effectively utilized to reduce NOx over the
lean NOx catalyst 30 while oxidizing the remaining HCs to release thermal
energy.
[0018] The combination of the lean NOx catalyst 30 and the NOx
absorber catalyst 32 overcomes the shortcomings of the individual
components. The so-configured optimized NOx exhaust system 14 enables
the lean NOx catalyst 30 and the NOx absorber catalyst 32 to each be half the
size if each were to be used individually. Because 75% of the NOx reduction
occurs in the first half of the catalyst, for both the lean NOx catalyst 30 and
the NOx absorber catalyst 32, reducing the size of each by half only reduces
the NOx conversion efficiency by 25%.
[0019] Both active and passive lean approaches can be
implemented based on the NOx conversion efficiency requirements and
engine out HCs. During the active approach, HC dosing in the exhaust and/or
in the cylinder (i.e., post combustion fuel injection) is enabled. Further, the
optimized NOx exhaust system enables tunable NOx conversion efficiency.
For example, if only 25 - 30% reduction is required under certain operating
conditions, only the lean NOx catalyst 30 is used, while the NOx absorber
catalyst 32 stays inactive. If higher efficiency is desired, the NOx absorber

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catalyst 32 is periodically regenerated to store and reduce NOx to nitrogen, as
well. As a result, fuel consumption is reduced. Further, the NOx absorber
catalyst also acts as a clean-up catalyst for N2O if so required.
[0020] During normal operation, if the engine out HC content is high
and NOx reduction demand is low, no active control is required. The
optimized NOx exhaust system 14 performs the required NOx reduction. If
the NOx reduction demand increases, the HC content is increased to
correspondingly increase the carbon to NOx ratio, thereby increasing the lean
NOx reduction efficiency. If further NOx reduction is desired, the NOx
absorber catalyst 32 can be periodically regenerated to store and convert
NOx to N2 In this manner, a wide range of NOx conversion is achieved,
which would otherwise not be possible with the lean NOx catalyst 30 or the
NOx absorber catalyst 32 alone. Also, fuel consumption can be reduced
because the HC rich exhaust for the NOx absorber catalyst regeneration is
not required all of the time. Further, because the NOx absorber catalyst 32 is
not used all of the time, its life is prolonged.
[0021] Referring now to Figure 2, exemplary steps executed by the
optimized NOx exhaust control will be described in detail. In step 200, control
determines whether the NOx reduction demand is less than a high threshold
(THRHI) (e.g., 75%). If the NOx reduction demand is not less than THRHI,
control regenerates the NOx absorber in step 202 and control ends. In this
manner, both the NOx absorber catalyst 32 and the lean NOx catalyst 30 are
implemented to achieve the higher conversion efficiency. If the NOx reduction
demand is not less than THRHI, control continues in step 204.
[0022] In step 204, control determines whether the NOx reduction
demand is less than a low threshold (THRLo) (e.g., 30%). If the NOx
reduction demand is not less than THRLO control increases the HC content of
the exhaust in step 206 and control ends. In this manner, the conversion
efficiency can be increased without regenerating the NOX absorber catalyst
32. If the NOx reduction demand is not less than THRLO, control uses the
lean NOx catalyst only in step 208 and control ends.

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[0023] Those skilled in the art can now appreciate from the
foregoing description that the broad teachings of the present invention can be
implemented in a variety of forms. Therefore, while this invention has been
described in connection with particular examples thereof, the true scope of the
invention should not be so limited since other modifications will become
apparent to the skilled practitioner upon a study of the drawings, the
specification and the following claims.

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CLAIMS
What is claimed is:
1. An exhaust after-treatment system for an internal combustion engine,
comprising:
a lean NOx catalyst having an exhaust stream from said internal
combustion engine flowing therethrough; and
a NOx absorber catalyst downstream of said lean NOx catalyst,
wherein said NOx absorber is selectively regenerated to increase a NOx
reduction efficiency of said exhaust after-treatment system.
2. The exhaust after-treatment system of claim 1 wherein said NOx
absorber catalyst is regenerated when a NOx reduction demand is greater
than a high threshold.
3. The exhaust after-treatment system of claim 1 wherein said lean NOx
catalyst alone reduces a NOx content of said exhaust stream when a NOx
reduction demand is less than a low threshold.
4. The exhaust after-treatment system of claim 1 wherein hydrocarbon
(HC) is introduced into said exhaust stream when a NOx reduction demand is
greater than a first threshold and is less than a second threshold.
5. The exhaust after-treatment system of claim 4 wherein said HC is
introduced via at least one of post-combustion in-cylinder fuel injection and in-
exhaust injection downstream of said internal combustion engine.
6. The exhaust after-treatment system of claim 1 further comprising a
hydrocarbon (HC) dosing unit disposed upstream of one of said lean NOx
catalyst and said NOx absorber catalyst.

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7. A method of reducing a NOx content of an exhaust stream exiting an
internal combustion engine, comprising:
directing said exhaust stream through a lean NOx catalyst to reduce
said NOx content of said exhaust stream;
directing said exhaust stream through a NOx absorber catalyst that is
disposed downstream of said lean NOx catalyst; and
selectively activating said NOx absorber catalyst to further reduce said
NOx content of said exhaust stream.
8. The method of claim 7 wherein said step of selectively activating
includes regenerating said NOx absorber catalyst to increase a NOx reduction
efficiency.
9. The method of claim 7 wherein said NOx absorber catalyst is activated
when a NOx reduction demand is greater than a high threshold.
10. The method of claim 7 wherein said lean NOx catalyst alone reduces a
NOx content of said exhaust stream when a NOx reduction demand is less
than a low threshold.
11. The method of claim 7 further comprising introducing hydrocarbon (HC)
into said exhaust stream when a NOx reduction demand is greater than a first
threshold and is less than a second threshold.
12. The method of claim 11 wherein said step of introducing said HC is
achieved via at least one of post-combustion in-cylinder fuel injection and in-
exhaust injection downstream of said internal combustion engine.
13. The method of claim 7 further comprising selectively injecting
hydrocarbon (HC) into said exhaust stream using a dosing unit that is
disposed upstream of one of said lean NOx catalyst and said NOx absorber
catalyst.

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14. A method of reducing a NOx content of an exhaust stream exiting an
internal combustion engine, comprising:
directing said exhaust stream through a lean NOx catalyst to reduce
said NOx content of said exhaust stream;
directing said exhaust stream through a NOx absorber catalyst that is
disposed downstream of said lean NOx catalyst;
selectively introducing hydrocarbon (HC) into said exhaust stream to
increase to further reduce said NOx content of said exhaust stream; and
selectively activating said NOx absorber catalyst to even further reduce
said NOx content of said exhaust stream.
15. The method of claim 14 wherein said step of selectively activating
includes regenerating said NOx absorber catalyst to increase a NOx reduction
efficiency.
16. The method of claim 14 wherein said NOx absorber catalyst is
activated when a NOx reduction demand is greater than a high threshold.
17. The method of claim 14 wherein said lean NOx catalyst alone reduces
a NOx content of said exhaust stream when a NOx reduction demand is less
than a low threshold.
18. The method of claim 14 wherein said step of introducing said HC is
achieved via at least one of post-combustion in-cylinder fuel injection and in-
exhaust injection downstream of said internal combustion engine.
19. The method of claim 14 wherein said step of selectively introducing HC
into said exhaust stream is achieved using a dosing unit that is disposed
upstream of one of said lean NOx catalyst and said NOx absorber catalyst.

An exhaust after-treatment system for an internal combustion engine
includes a lean NOx catalyst having an exhaust stream from the internal
combustion engine flowing therethrough. A NOx absorber catalyst is
downstream of the lean NOx catalyst. The NOx absorber is selectively
regenerated to increase a NOx reduction efficiency of the exhaust after-
treatment system.

Documents:

00942-kol-2007-abstract.pdf

00942-kol-2007-assignment.pdf

00942-kol-2007-claims.pdf

00942-kol-2007-correspondence others 1.1.pdf

00942-kol-2007-correspondence others 1.2.pdf

00942-kol-2007-correspondence others.pdf

00942-kol-2007-description complete.pdf

00942-kol-2007-drawings.pdf

00942-kol-2007-form 1.pdf

00942-kol-2007-form 2.pdf

00942-kol-2007-form 3.pdf

00942-kol-2007-form 5.pdf

00942-kol-2007-priority document.pdf

942-KOL-2007-(11-09-2012)-ABSTRACT.pdf

942-KOL-2007-(11-09-2012)-AMANDED CLAIMS.pdf

942-KOL-2007-(11-09-2012)-ANNEXURE TO FORM 3.pdf

942-KOL-2007-(11-09-2012)-DESCRIPTION (COMPLETE).pdf

942-KOL-2007-(11-09-2012)-DRAWINGS.pdf

942-KOL-2007-(11-09-2012)-EXAMINATION REPORT REPLY RECEIVED.pdf

942-KOL-2007-(11-09-2012)-FORM-1.pdf

942-KOL-2007-(11-09-2012)-FORM-2.pdf

942-KOL-2007-(11-09-2012)-OTHERS.pdf

942-KOL-2007-CORRESPONDENCE OTHERS-1.3.pdf

942-KOL-2007-CORRESPONDENCE-1.4.pdf

942-kol-2007-form 18.pdf

942-KOL-2007-PA.pdf


Patent Number 256243
Indian Patent Application Number 942/KOL/2007
PG Journal Number 21/2013
Publication Date 24-May-2013
Grant Date 22-May-2013
Date of Filing 29-Jun-2007
Name of Patentee GM GLOBAL TECHNOLOGY OPERATIONS, INC
Applicant Address 300 GM RENAISSANCE CENTER DETROIT, MICHIGAN
Inventors:
# Inventor's Name Inventor's Address
1 RAHUL MITAL 2706 BROADMOOR DRIVE ROCHESTER HILLS, MICHIGAN 48309
PCT International Classification Number F01N3/20; F01N9/00
PCT International Application Number N/A
PCT International Filing date
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 11/466,927 2006-08-24 U.S.A.