WO2011103157A2

WO2011103157A2 - On-vehicle nitrogen oxide aftertreatment system

Info

Publication number: WO2011103157A2
Application number: PCT/US2011/025043
Authority: WO
Inventors: Gabriel Salanta; Timothy Jackson; Henry Sullivan; Adam J. Kotrba
Original assignee: Tenneco Automotive Operating Co Inc
Current assignee: Tenneco Automotive Operating Co Inc
Priority date: 2010-02-17
Filing date: 2011-02-16
Publication date: 2011-08-25
Anticipated expiration: 2012-08-17
Also published as: CN102713179A; US20110197569A1; DE112011100576T5; KR101487178B1; JP2013519842A; US8381514B2; WO2011103157A3; KR20130008526A; BR112012019611A2

Abstract

An emissions system for reducing nitrogen oxides in engine exhaust includes an emissions catalyst having an inlet adapted to receive an exhaust from the engine. A fuel tank is adapted to provide fuel for combustion within the engine. A first injector is operable to inject fuel into the exhaust upstream of the catalyst. A second injector is operable to inject supplemental reductant from a supplemental reductant tank into the exhaust upstream of the catalyst. A controller is operable to control the first and second injectors and vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust.

Description

ON-VEHICLE NITROGEN OXIDE AFTERTREATMENT SYSTEM

CROSS-REFERENCE TO RELATED APPLICATIONS

[0001] This application claims priority to U.S. Application No. 12/773,314, filed on May 4, 2010, which claims the benefit of U.S. Provisional Application No. 61 /305,272, filed on February 17, 2010. The entire disclosure of the above applications are incorporated herein by reference.

BACKGROUND

[0002] Selective catalytic reduction technology has been used in conjunction with reducing nitrogen oxides present in the exhaust of internal combustion engines. Many vehicles utilizing internal combustion engines as a prime mover are also equipped with exhaust aftertreatment devices for reducing nitrogen oxide emissions. Some of these systems are constructed using urea- based technology including a separate container mounted to the vehicle for storing the urea, a urea injector and a selective catalytic reduction catalyst. While these systems may have performed well in the past, it may be desirable to provide a selective catalytic reduction system operable without the use of urea or other reductants not typically onboard a vehicle.

SUMMARY

[0003] This section provides a general summary of the disclosure, and is not a comprehensive disclosure of its full scope or all of its features.

[0004] An emissions system for reducing nitrogen oxides in engine exhaust includes an emissions catalyst having an inlet adapted to receive an exhaust from the engine. A fuel tank is adapted to provide fuel for combustion within the engine. A first injector is operable to inject fuel into the exhaust upstream of the catalyst. A second injector is operable to inject supplemental reductant from a supplemental reductant tank into the exhaust upstream of the catalyst. A controller is operable to control the first and second injectors and vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust. [0005] An emissions system for reducing nitrogen oxides in engine exhaust includes an emissions catalyst having an inlet adapted to receive an exhaust from the engine. An injector is operable to inject a reductant into the exhaust upstream of the catalyst. A fuel tank is adapted to provide fuel for combustion within the engine. A valve is supplied fuel from the fuel tank. The valve is also in receipt of a reductant from a supplemental reductant tank. The valve is operable to selectively supply one or both of the fuel and the supplemental reductant to the injector to reduce nitrogen oxides within the exhaust.

[0006] An emissions system includes an emissions catalyst having an inlet adapted to receive an exhaust from an engine. A first injector is operable to inject fuel from a fuel tank into the exhaust upstream of the catalyst. The fuel tank also provides fuel for combustion in the engine. A second injector is operable to inject supplemental reductant stored in a supplemental reductant tank into the exhaust upstream of the catalyst. A burner is in receipt of the exhaust and positioned upstream from the first and second injectors. A diesel particulate filter is positioned downstream of the burner and upstream of the first and second injectors. A controller is operable to control the burner as well as the first and second injectors to vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust.

[0007] Further areas of applicability will become apparent from the description provided herein. The description and specific examples in this summary are intended for purposes of illustration only and are not intended to limit the scope of the present disclosure.

DRAWINGS

[0008] The drawings described herein are for illustrative purposes only of selected embodiments and not all possible implementations, and are not intended to limit the scope of the present disclosure.

[0009] Figure 1 is a schematic view of a selective catalytic reduction

(SCR) system with multiple reductants on a vehicle; [0010] Figure 2 is a graph depicting N0_X conversion versus temperature using E85 as a reductant with different catalysts;

[0011] Figure 3 is a graph depicting ΝΟχ reduction percentage versus a ratio of hydrocarbon to NOx using diesel fuel as a reductant;

[0012] Figure 4 is a graph depicting NO_x reduction at various reductant ratios;

[0013] Figure 5 is a schematic view of an alternate selective catalytic reduction (SCR) system with multiple reductants on a vehicle;

[0014] Figure 6 is a schematic view of another alternate selective catalytic reduction (SCR) system with multiple reductants on a vehicle; and

[0015] Figure 7 is a schematic view of another alternate selective catalytic reduction (SCR) system with multiple reductants on a vehicle.

[0016] Corresponding reference numerals indicate corresponding parts throughout the several views of the drawings.

DETAILED DESCRIPTION

[0017] Example embodiments will now be described more fully with reference to the accompanying drawings.

[0018] Figure 1 depicts an exhaust treatment system 10 associated with an exemplary vehicle 12. Vehicle 12 includes an engine 14 arranged as a prime mover having an exhaust port 16 in fluid communication with an exhaust pipe 18. Engine exhaust flows through pipe 18 in the direction indicated by the arrow. An injector 20 is positioned to inject a reductant into the engine exhaust flowing through exhaust pipe 18. An emissions catalyst 22 is positioned downstream of injector 20 and is in receipt of engine exhaust flowing through pipe 18.

[0019] A fuel tank 26 is mounted to vehicle 12 to store fuel. Fuel tank 26 is in communication with engine 14 via a fuel supply line 27 such that fuel may be selectively supplied to combustion chambers of engine 14. It is contemplated that engine 14 may be a gasoline fueled spark ignition engine or may be a diesel fueled compression engine. Fuels for the gasoline engine may include gasoline, E85, E95 or other similar fuels. Fuels for the diesel engine may include diesel fuel, biofuel B5, B10, B20 or other similar fuels. A supplemental reductant tank 28 is also mounted to vehicle 12. It is contemplated that tank 28 may store a readily available reductant such as E85, E95, B5, B10, B20 or the like.

[0020] A valve 30 selectively interconnects injector 20 with one or both of fuel tank 26 and supplemental reductant tank 28. More particularly, a first supply line 32 extends from fuel tank 26 to a first inlet port 34 of valve 30. In similar fashion, a second supply line 36 interconnects tank 28 and a second inlet port 38 of valve 30.

[0021] A controller 40 is operable to control valve 30 to selectively supply reductant to injector 20. Controller 40 may cause valve 30 to solely provide fuel from tank 26 to injector 20. Depending on the conditions present, fuel may act as a suitable reductant. Controller 40 may also control valve 30 to solely supply the reductant stored within supplemental reductant tank 28 to injector 20. Controller 40 may simultaneously provide fuel and a supplemental reductant to injector 20 at one of any number of mixing ratios between 0 - 100%.

[0022] A plurality of sensors 42 may be in communication with controller 40 such that the signal provided to control valve 30 is based on an evaluation of vehicle data. Sensors 42 may provide signals indicative of, but not limited to, engine speed, engine operating temperature, exhaust temperature, mass air flow, diesel fuel volume within tank 26, reductant volume within tank 28, ΝΟχ concentration, HC concentration, 0₂ concentration, H₂ concentration, ammonia concentration and other data that may be available from a CAN bus or dedicated sensors mounted to vehicle 12. Based on the input provided from sensors 42, controller 40 selectively operates injector 20 by injecting the reductant flowing through valve 30.

[0023] Figure 2 depicts ΝΟχ conversion versus temperature having E85 as a reductant used in cooperation with two different catalysts. Catalyst A and catalyst B represent two known catalysts used for selective catalytic reduction in urea-based systems. It should be noted that relatively high NO_x conversion is depicted while using E85 as the reductant with either catalyst. The graph depicts a merely exemplary and non-limiting example of E85 concentration where the hydrocarbon to NO_x ratio is five.

[0024] Figure 3 depicts ΝΟχ reduction percent versus a ratio of hydrocarbon to ΝΟχ while using diesel fuel as a reductant. ΝΟχ reduction ranges from approximately 38% to 56% as the ratio of hydrocarbon to NO_x ranges from 4-8 at an operating temperature of approximately 350°C. NO_x reduction ranges from approximately 28 - 47% as the ratio of hydrocarbon to ΝΟχ varies from 4-6 at an operating temperature of approximately 400 °C. Based on the dual reductant source and valve arrangement shown in Figure 1 , it should be appreciated that effective NOx reduction may be achieved solely through the use of E85 as a reductant. ΝΟχ reduction may also be achieved through the use of engine fuel as a reductant.

[0025] It is also contemplated that two or more different reductants may be simultaneously injected into the exhaust stream to effectively convert ΝΟχ in the exhaust stream to N₂. Figure 4 depicts ΝΟχ reduction at various reductive ratios where a first reductant includes E100 and a second reductant includes ultra-low sulfur diesel (ULSD). Percentage NO_x reduction was determined for several different reductant ratios where E100 and ULSD were simultaneously injected into an exhaust stream. A first ΝΟχ reduction percentage was determined using E100 at a carbon to nitrogen ratio of 1 being simultaneously injected with ULSD having a carbon to nitrogen ratio of 5. A second NOx reduction percentage was determined using the reductant ratio of E100 having a carbon to nitrogen ratio of 3 being simultaneously injected with ULSD having a carbon to nitrogen ratio of 3. At the far right of the chart shown in Figure 4, a different reduction ratio was evaluated for NO_x reduction effectiveness. E100 at a carbon to nitrogen ratio of 3 was simultaneously injected with ULSD having a carbon to nitrogen ratio of 6. The second data point from the right shown in Figure 4 corresponds to 100% E85 being injected at a carbon to nitrogen ratio of 5.

[0026] Figures 2, 3 and 4 illustrate that it may beneficial to determine a ratio of primary and secondary reductant dynamically in response to engine operating conditions. In particular, it may be desirable to monitor an engine exhaust temperature at one or more locations relative to a catalyst. Furthermore, controller 40 may be programmed to estimate a carbon to nitrogen ratio of one or more reductants stored on board vehicle 12. Based on the ΝΟχ reduction percentages obtained during various reductant ratios and exhaust temperatures, controller 40 may optimize the use of reductant stored within tank 28. Controller 40 may also evaluate other vehicle operating conditions including throttle position, engine speed and vehicle speed to set a target ΝΟχ reduction percentage and subsequently determine a desired reductant injection ratio.

[0027] Figure 5 depicts an alternate exhaust treatment system 100. Exhaust treatment system 100 is substantially similar to exhaust treatment system 10. Accordingly, like elements will retain their previously introduced reference numerals. Exhaust treatment system 100 includes fuel tank 26 and supplemental reductant tank 28. A fuel supply line 102 interconnects fuel tank 26 and a first injector 104. First injector 104 is operable to selectively supply fuel as a reductant to the engine exhaust flow in pipe 18. The supply of fuel into the exhaust stream is controlled by controller 40.

[0028] Another supply line 106 interconnects reductant tank 28 with a second injector 108. Second injector 108 is selectively operable to inject the reductant contained within tank 28 into the exhaust stream passing through exhaust pipe 18. It should be appreciated that while first injector 104 is depicted as being upstream of second injector 108 in Figure 4, this relative position may be reversed or first injector 104 may be positioned at substantially the same distance from emissions catalyst 22 as second injector 108. To achieve this arrangement, the injectors may be positioned at different rotational clocking orientations about exhaust pipe 18. Controller 40 is also in communication with second injector 108 to define and control when reductant stored within tank 28 is to be supplied to the exhaust flowing through exhaust pipe 18.

[0029] Figure 6 depicts another alternate exhaust treatment system identified at reference numeral 200. Exhaust treatment system 200 is substantially similar to exhaust treatment system 100. Accordingly, like elements will retain their previously introduced reference numerals. Exhaust treatment system 200 includes each of the elements of exhaust treatment system 100 as well as a thermal management device 202 positioned upstream from first injector 104 and second injector 108. Thermal management device 202 may include a burner 204 for increasing the temperature of exhaust flowing through exhaust pipe 18. Thermal management device 202 may also include a diesel particulate filter 206. Thermal management device 202 may include both burner 204 and diesel particulate filter 206.

[0030] Burner 204 may include an injector 208 operable to supply an ignitable fuel to the exhaust stream. An additional source of oxygen may be provided by a pressurized air source 209. An igniter 210 may also be provided as part of burner 204 to selectively ignite fuel that may be within the exhaust flowing through exhaust pipe 18 with or without additional fuel being supplied via injector 208. When burner 204 is used in combination with diesel particulate filter 206, the filter may be actively regenerated by energizing burner 204 to burn soot previously collected by diesel particulate filter 206. Controller 40 is operable to control igniter 210 and injector 208 to define when burner 204 heats the exhaust.

[0031] Figure 7 illustrates another alternate exhaust treatment system identified at reference numeral 300. Exhaust treatment system 300 is substantially similar to exhaust treatment system 200. Accordingly, like elements will retain their previously introduced reference numerals. Exhaust treatment system 300 includes each of the elements of exhaust treatment system 200 as well as an additional catalyst 302 positioned in series with and downstream from catalyst 22. Reductant tank 26 provides reductant to first injector 104 upstream of catalyst 22. Reductant tank 28 provides reductant to second injector 108 downstream of catalyst 22 and upstream of catalyst 302. It is contemplated that catalyst 22 and catalyst 302 are substantially similar to one another. The use of two catalysts in series may provide an increased ΝΟχ reduction percentage and longer catalyst life for each of catalyst 22 and catalyst 302.

[0032] The use of diesel fuel as a reductant may increase the likelihood of coking within the catalyst immediately downstream from the diesel fuel reductant injector. Figure 7 depicts diesel fuel as the reductant stored within tank 26 and provided to first injector 104. Thermal management device 202 is positioned closest to catalyst 22 in receipt of diesel fuel as the reductant. The increased temperature of the exhaust may minimize the coking and assist with catalyst regeneration, if desired. During operation, first injector 104 and second injector 108 may be individually operated or simultaneous reductant injection may occur depending on the engine operating conditions, as previously discussed.

[0033] In an alternate arrangement, an optional valve 304 may be operable to supply the reductant within fuel tank 26 to second injector 108 and provide the reductant within tank 28 to first injector 104. A switching of the reductant supply may facilitate regeneration of catalyst 22 and/or catalyst 302. A switching of reductants may increase the life of both catalyst 22 and catalyst 302. It should also be appreciated that the concepts of the present disclosure may be utilized in conjunction with engines outputting large volumes of exhaust per unit time. Some exhaust systems include multiple parallel conduits in communication with the engine. It is within the scope of the present disclosure to use multiple sets of injectors and/or valves to duplicate the previously described exhaust gas treatment systems along more than one of the parallel exhaust conduits.

[0034] The foregoing description of the embodiments has been provided for purposes of illustration and description. It is not intended to be exhaustive or to limit the disclosure. Individual elements or features of a particular embodiment are generally not limited to that particular embodiment, but, where applicable, are interchangeable and can be used in a selected embodiment, even if not specifically shown or described. The same may also be varied in many ways. Such variations are not to be regarded as a departure from the disclosure, and all such modifications are intended to be included within the scope of the disclosure.

Claims

CLAIMS What is claimed is:

1 . An emissions system for reducing nitrogen oxides in engine exhaust, the system comprising:

an emissions catalyst having an inlet adapted to receive an exhaust from the engine;

an injector operable to inject a reductant into the exhaust upstream of the catalyst;

a fuel tank adapted to provide fuel for combustion within the engine;

a supplemental reductant tank; and

a valve being supplied fuel from the fuel tank as a first reductant, the valve also being in receipt of a second reductant from the supplemental reductant tank, wherein the valve is operable to selectively supply one or both of the first and second reductants to the injector to reduce nitrogen oxides within the exhaust.

2. The emissions system of claim 1 wherein the fuel includes one of gasoline, E85 and E95.

3. The emissions system of claim 1 wherein the fuel includes one of diesel fuel, biofuel B5, biofuel B10 and biofuel B20.

4. The emissions system of claim 1 wherein the second reductant includes one of E85, E95, B5, B10 and B20.

5. The emissions system of claim 1 further including a controller for controlling the injector and selectively injecting reductant into the exhaust.

6. The emissions system of claim 5 wherein the controller controls the valve based on input from vehicle sensors.

7. An emissions system for reducing nitrogen oxides in engine exhaust, the system comprising:

a fuel tank adapted to provide fuel for combustion within the engine;

a first injector operable to inject fuel into the exhaust upstream of the catalyst;

a supplemental reductant tank;

a second injector operable to inject supplemental reductant into the exhaust upstream of the catalyst; and

a controller operable to control the first and second injectors and vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust.

8. The emissions system of claim 7 wherein the fuel includes one of gasoline, E85 and E95.

9. The emissions system of claim 7 wherein the fuel includes one of diesel fuel, biofuel B5, biofuel B10 and biofuel B20.

10. The emissions system of claim 7 wherein the supplemental reductant includes one of E85, E95, B5, B10 and B20.

1 1 . The emissions system of claim 7 further including a burner in receipt of the exhaust and positioned upstream from the first and second injectors.

12. The emissions system of claim 1 1 further including a diesel particulate filter positioned downstream of the burner and upstream of the first and second injectors.

13. The emissions system of claim 7 wherein the first and second injectors simultaneously inject reductant into the exhaust.

14. An emissions system for reducing nitrogen oxides in engine exhaust, the system comprising:

a fuel tank adapted to provide fuel for combustion within the engine;

a supplemental reductant tank;

a second injector operable to inject supplemental reductant into the exhaust upstream of the catalyst;

a burner in receipt of the exhaust and positioned upstream from the first and second injectors;

a diesel particulate filter positioned downstream of the burner and upstream of the first and second injectors; and

a controller operable to control the burner as well as the first and second injectors to vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust.

15. The emissions system of claim 14 wherein the fuel includes one of gasoline, E85 and E95.

16. The emissions system of claim 14 wherein the supplemental reductant includes one of E85, E95, B5, B10 and B20.

17. An emissions system for reducing nitrogen oxides in engine exhaust, the system comprising:

a first emissions catalyst having an inlet adapted to receive an exhaust from the engine; a second emissions catalyst having an inlet adapted to receive an exhaust from the first emissions catalyst;

a fuel tank adapted to provide fuel for combustion within the engine;

a first injector operable to inject fuel into the exhaust upstream of the first catalyst;

a supplemental reductant tank;

a second injector operable to inject supplemental reductant into the exhaust upstream of the second catalyst and downstream of the first catalyst; and

a burner in receipt of the exhaust and positioned upstream from the first and second injectors.

18. The emissions system of claim 17 further including a controller operable to control the burner as well as the first and second injectors to vary the supply of fuel and supplemental reductant into the exhaust to reduce nitrogen oxides within the exhaust.

19. The emissions system of claim 18 further including a valve operable to provide fuel to the second injector and supplemental reductant to the first injector.