An exhaust system conducts hot exhaust gases generated by an engine through various exhaust components to reduce emissions and control noise. The exhaust system includes an injection system that injects a diesel exhaust fluid (DEF) or a reducing agent, such as a solution of urea and water for example, upstream of a selective catalytic reduction (SCR) catalyst. A mixer is positioned upstream of the SCR catalyst and mixes engine exhaust gases and products of urea transformation. The injection system includes a doser that sprays the urea into the exhaust stream. The urea should be transformed as much as possible into ammonia (NH3) before reaching the SCR catalyst. Thus, the droplet spray size plays an important role in reaching this goal.
In one known configuration, the mixer includes an outer housing with an opening that receives the doser. A cone is aligned with this opening to provide a widening spray area into the internal cavity of the outer housing. The widening spray area facilitates a more thorough distribution of spray droplets over a larger area as the spray enters the exhaust gas stream.
The industry is moving towards providing more compact exhaust systems, which results in reduced volume of the system. Systems that spray larger size droplets may not be able to provide adequate transformation of urea when used in more compact system configurations. As such, smaller droplet size dosers are required for these more compact configurations.
The smaller the droplet size, the more effective the transformation into ammonia is, due to the increased surface contact area. However, the spray generated by small droplet dosers is very sensitive to recirculation flow. Typically, an area located at a tip of the doser has a vortex of recirculating flow. This vortex pushes the spray droplets towards the walls of the mixer and onto the tip of the doser, which creates deposit initiation sites. In configurations that utilize a cone, deposit initiation sites have been found on the wall of the cone. The deposits in these sites build up over time and can adversely affect system operation. For example, there may be a lower ammonia uniformity index, there may be an increased pressure drop across the mixer, or they may be a peak of ammonia emissions during active diesel particulate filter (DPF) regeneration.
In one exemplary embodiment, a mixer for a vehicle exhaust system includes an outer housing having an upstream end and a downstream end. An upstream baffle has an inlet opening configured to receive exhaust gas and is mounted at the upstream end of the outer housing. A downstream baffle has an outlet opening configured to conduct exhaust gases to a downstream exhaust component and is mounted at the downstream end of the outer housing. A doser opening is formed within the outer housing at a location between the upstream and downstream baffles. A cone has a narrow end with an inlet opening and a wide end with an outlet opening. A tapered body portion extends from the narrow end to the wide end, with the cone being aligned with the doser opening. An extension portion extends outwardly from the wide end of the cone and provides a wall that surrounds the outlet opening.
In a further embodiment of the above, the extension portion and the cone are integrally formed together as a single-piece component.
In a further embodiment of any of the above, a curved transition surface extends from an inner surface of the cone at the wide end to the extension portion.
In a further embodiment of any of the above, the extension portion further includes a wall portion overlapping an inner peripheral surface of the outer housing and a plate portion extending radially inwardly from the wall portion.
In another exemplary embodiment, a vehicle exhaust system comprises a mixer having an upstream baffle with at least one inlet opening configured to receive engine exhaust gas, a downstream baffle with at least one outlet opening configured to conduct engine exhaust gases to a downstream exhaust component, an outer peripheral wall surrounding the upstream and downstream baffles and defining a mixer central axis. A doser is configured to spray a reducing agent into the mixer, the doser defining a central doser axis and being mounted at a doser opening within the outer peripheral wall. A cone has a narrow end with an inlet opening and a wide end with an outlet opening. A tapered body portion extends from the narrow end to the wide end, the cone being aligned with the doser opening. An extension portion extends outwardly from the wide end of the cone to provide a wall that surrounds the outlet opening.
In a further embodiment of any of the above, the central doser axis does not intersect the central mixer axis.
These and other features of this application will be best understood from the following specification and drawings, the following of which is a brief description.
In one example configuration, the upstream exhaust components 14 direct exhaust gases into a diesel oxidation catalyst (DOC) 16 having an inlet 18 and an outlet 20. Downstream of the DOC 16 is an optional component 21 that may be a diesel particulate filter (DPF), which is used to remove contaminants from the exhaust gas as known. In one example, the component 21 may be the DPF and a subsequent portion of exhaust pipe with an optional elbow type connection. In another example, the component 21 may be a portion of exhaust pipe with an optional elbow type connection. Downstream of the DOC 16 and optional component 21 is a selective catalytic reduction (SCR) catalyst 22 having an inlet 24 and an outlet 26. The outlet 26 communicates exhaust gases to downstream exhaust components 28. Optionally, component 22 can comprise a catalyst that is configured to perform a selective catalytic reduction function and a particulate filter function. The various downstream exhaust components 28 can include one or more of the following: pipes, filters, valves, catalysts, mufflers etc. These upstream 14 and downstream 28 components can be mounted in various different configurations and combinations dependent upon vehicle application and available packaging space.
A mixer 30 is positioned downstream from the outlet 20 of the DOC 16 or component 21 and upstream of the inlet 24 of the SCR catalyst 22. The upstream catalyst and downstream catalyst can be in-line, in parallel or any other configuration. The mixer 30 (as shown in the in-line configuration) is used to generate a swirling or rotary motion of the exhaust gas. An injection system 32 is used to inject a gaseous or liquid reducing agent, such as a solution of urea and water for example, into the exhaust gas stream upstream from the SCR catalyst 22 such that the mixer 30 can mix the injected substance and exhaust gas thoroughly together. In an example, the injection system 32 includes a fluid supply 34, a doser 36, and a controller 38 that controls injection of the reducing agent as known. Optionally, component 36 can be a pipe of introduction of gaseous reducing agent. Operation of the controller 38 to control injection of the reducing agent is known and will not be discussed in further detail.
The mixer 30 is shown in greater detail in
The upstream baffle 50 at the inlet 42 may include a large inlet opening 60 that can receives the majority of the exhaust gas (for example, the large inlet opening 60 receives 60% of the exhaust mass flow rate), and which is configured to initiate the swirling motion. The upstream baffle 50 also includes a plurality of perforations, slots, or additional inlet openings 62 that ensure optimal homogenization of exhaust gases and reduces back pressure. The upstream baffle 50 and the plurality of inlet openings 60, 62 cooperate to initiate a swirling motion to the exhaust gas as the exhaust gas enters the inlet end 42 of the mixer 30.
The downstream baffle 52 includes a large outlet opening 64 (
The large outlet opening 64 comprises primary outlet opening and is larger than the other outlet openings 66. The helical portion 70 includes the additional outlet openings 66. The helical portion 70 is formed by an upstream end portion 74 and a downstream end portion 78. Portions 74 and 78 include flat surface portions perpendicular to the mixer axis A (
Similarly, as shown in
The outer peripheral wall 54 includes an opening 92 formed at a location between the upstream 50 and downstream 52 baffles. The opening 92 is configured to receive the doser 36.
As best shown in
The intermediate plate 100 is attached to the manifold 98 and the cone 96 to form the sub-assembly 94. The intermediate plate 100 has an apex 102 near the mixer central axis A and which widens radially outward in a direction toward the outer peripheral wall 54. The intermediate plate 100 comprises a flat portion 104 defined by a first edge 106 extending radially outward from the apex 102, a second edge 108 extending radially outward from the apex 102 and circumferentially spaced from the first edge 106, and an outer peripheral edge 110 connecting the first 106 and second 108 edges to define a wedge-shape. The first edge 106 comprises an inlet side of the intermediate plate 100 and the second edge 108 comprises the outlet side of the intermediate plate 100. The angle defined by edge 106 and edge 108 can vary from 70 deg to 270 deg. The flat portion 104 can have an adjacent helical portion at the outlet side, which is the edge 108.
In one example, the intermediate plate 100 includes a flange portion 112 that extends in an upstream direction from the outer peripheral edge 110. The flange portion 112 does not extend along the entire outer peripheral edge 110. As shown in
The sub-assembly 94 is then placed within the mixer 30, as shown in
As best shown in
In the example shown in
The cone 200 is attached to a manifold 220 (
The intermediate plate 100 and plate portion 212 for these example embodiments, are positioned between the upstream 50 and downstream 52 baffles to block direct flow from the primary inlet opening 60 to the primary outlet opening 64. This blockage provides for a rotational flow path that directs exhaust gases exiting the primary inlet opening 60 through a rotation of more than 360 degrees about the mixer central axis A before exiting the primary outlet opening 64. This increased degree of rotation results in more thorough mixing of the reducing agent within the exhaust gas. Also, this more thorough mixing occurs without having to increase the overall axial mixer length according to the axis A direction.
Thus, the subject invention provides a compact mixer 30 that allows at least 360 degrees of flow path in order to increase mixing performance and enhance DEF transformation when a liquid reducing agent is used. Additionally, by providing an integrated doser cone 96, a smooth transition is provided at the interface between the cone outlet and inner mixer wall resulting in reduced deposit formation, which further improves performance. This improved performance is provided without increasing the axial length of the mixer and, further, does not adversely affect back pressure. For example, this 360 to 450 degree rotation flow path is provided within a mixer having an overall length that is 7 to 10 inches long according to the direction defined by axis A.
Although an embodiment of this invention has been disclosed, a worker of ordinary skill in this art would recognize that certain modifications would come within the scope of this invention. For that reason, the following claims should be studied to determine the true scope and content of this invention.
This application claims priority to U.S. Provisional Patent Application No. 62/155,025, filed Apr. 30, 2015.
Number | Name | Date | Kind |
---|---|---|---|
5606856 | Linder | Mar 1997 | A |
6539708 | Hofmann | Apr 2003 | B1 |
8438839 | Floyd | May 2013 | B2 |
8800276 | Levin | Aug 2014 | B2 |
9057312 | Munnannur | Jun 2015 | B2 |
9180407 | De Rudder | Nov 2015 | B2 |
20030110763 | Pawson | Jun 2003 | A1 |
20030226412 | Rumminger | Dec 2003 | A1 |
20060070374 | Gaiser | Apr 2006 | A1 |
20060218902 | Arellano | Oct 2006 | A1 |
20070092413 | Hirata | Apr 2007 | A1 |
20070163241 | Meingast | Jul 2007 | A1 |
20070193252 | McKinley | Aug 2007 | A1 |
20080011777 | Cooke | Jan 2008 | A1 |
20080011780 | Cooke | Jan 2008 | A1 |
20080022670 | Ichikawa | Jan 2008 | A1 |
20080092526 | Kunkel | Apr 2008 | A1 |
20080163612 | Gaiser | Jul 2008 | A1 |
20080282687 | Park | Nov 2008 | A1 |
20090044524 | Fujino | Feb 2009 | A1 |
20090084094 | Goss | Apr 2009 | A1 |
20090107126 | Bugos et al. | Apr 2009 | A1 |
20090120066 | VanderGriend | May 2009 | A1 |
20090127511 | Bruck | May 2009 | A1 |
20100005790 | Zhang | Jan 2010 | A1 |
20100071355 | Brown | Mar 2010 | A1 |
20100101222 | Oesterle | Apr 2010 | A1 |
20100186393 | Kowada | Jul 2010 | A1 |
20100212292 | Rusch et al. | Aug 2010 | A1 |
20110094206 | Liu et al. | Apr 2011 | A1 |
20110107743 | Ranganathan | May 2011 | A1 |
20120216513 | Greber et al. | Aug 2012 | A1 |
Number | Date | Country |
---|---|---|
4417238 | Mar 2003 | DE |
19806265 | Jul 2004 | DE |
10312212 | Sep 2006 | DE |
102005061145 | Jun 2007 | DE |
202007010324 | Nov 2008 | DE |
102007051510 | Apr 2009 | DE |
102007052262 | May 2009 | DE |
202008001022 | Jun 2009 | DE |
102008008563 | Aug 2009 | DE |
102008008564 | Aug 2009 | DE |
102008040476 | Apr 2013 | DE |
10241697 | May 2016 | DE |
0268026 | Aug 1993 | EP |
1314864 | Jan 2007 | EP |
2221459 | Aug 2010 | EP |
2282026 | Feb 2011 | EP |
2295755 | Mar 2011 | EP |
2405109 | Jan 2012 | EP |
2492465 | Aug 2012 | EP |
2465602 | Nov 2013 | EP |
2687286 | Jan 2014 | EP |
2295756 | Mar 2014 | EP |
2860369 | Apr 2015 | EP |
2860370 | Apr 2015 | EP |
2325452 | May 2015 | EP |
2884069 | Jun 2015 | EP |
2980379 | Feb 2016 | EP |
2897646 | Aug 2008 | FR |
2965011 | Mar 2012 | FR |
2977632 | Jan 2013 | FR |
H2223624 | Feb 1989 | JP |
H0296212 | Apr 1990 | JP |
2013002367 | Jan 2013 | JP |
20110049152 | May 2011 | KR |
531199 | Jan 2009 | SE |
9701387 | Jan 1997 | WO |
2008027146 | Mar 2008 | WO |
2008034981 | Mar 2008 | WO |
2009068136 | Jun 2009 | WO |
2010078052 | Jul 2010 | WO |
2011056676 | May 2011 | WO |
2011106487 | Sep 2011 | WO |
2011110885 | Sep 2011 | WO |
2011139953 | Nov 2011 | WO |
2011163395 | Dec 2011 | WO |
2012013562 | Feb 2012 | WO |
2012044233 | Apr 2012 | WO |
2012047159 | Apr 2012 | WO |
2012050509 | Apr 2012 | WO |
2012052560 | Apr 2012 | WO |
2012053960 | Apr 2012 | WO |
2012054437 | Apr 2012 | WO |
2012096971 | Jul 2012 | WO |
2012120000 | Sep 2012 | WO |
2013010700 | Jan 2013 | WO |
2013035112 | Mar 2013 | WO |
2013036406 | Mar 2013 | WO |
2013048309 | Apr 2013 | WO |
2013099312 | Jul 2013 | WO |
2013099313 | Jul 2013 | WO |
2013099314 | Jul 2013 | WO |
2013112154 | Aug 2013 | WO |
2013178321 | Dec 2013 | WO |
2014017310 | Jan 2014 | WO |
2014047091 | Mar 2014 | WO |
2014051617 | Apr 2014 | WO |
2014051617 | Apr 2014 | WO |
2014077023 | May 2014 | WO |
2014112063 | Jul 2014 | WO |
2014112067 | Jul 2014 | WO |
2014112073 | Jul 2014 | WO |
2014182832 | Nov 2014 | WO |
2015018971 | Feb 2015 | WO |
2015020820 | Feb 2015 | WO |
2015074926 | May 2015 | WO |
2015076765 | May 2015 | WO |
2015130640 | Sep 2015 | WO |
2015151282 | Oct 2015 | WO |
2015187128 | Dec 2015 | WO |
2016013319 | Jan 2016 | WO |
2014112072 | Jan 2017 | WO |
2014115461 | Jan 2017 | WO |
Entry |
---|
International Search Report and Written Opinion for International Application No. PCT/US2016/028237 mailed Jul. 28, 2016. |
International Search Report for PCT International Application Serial No. PCT/US2016/058114, 16FECT013 PCT ||, 9 pages. |
Jean et al., New Concepts for the Urea Injection Area in SCR Exhaust Systems for Passenger Cars, Aachen Congress, p. 1373-2010, 2010, 18 pages. |
Rusch et al., Urea SCR Interaction of Spray Generation and Exhaust System, 3rd International CTI Forum SCR-System, Bonn, Apr. 2008, 30 pages. |
Number | Date | Country | |
---|---|---|---|
20160319723 A1 | Nov 2016 | US |
Number | Date | Country | |
---|---|---|---|
62155025 | Apr 2015 | US |