This application claims the benefit of priority under 35 U.S.C. §119 of German Patent Application 10 2007 028 449.9 filed Jun. 18, 2008, the entire contents of which are incorporated herein by reference.
The present invention pertains to a mixing and/or evaporating device for an exhaust system of an internal combustion engine, especially in a motor vehicle. The present invention pertains, in addition, to a process for manufacturing such a mixing and/or evaporating device as well as an exhaust system equipped with such a mixing and/or evaporating device.
It may be necessary for various reasons in exhaust systems of internal combustion engines to inject a liquid educt into the exhaust gas stream. For example, fuel may be injected into the exhaust gas stream upstream of an oxidation catalyst in order to induce an exothermal combustion reaction at an oxidation catalyst arranged downstream. For example, a reducing agent, e.g., ammonia, may likewise also be injected into the exhaust gas stream in order to reduce nitrogen oxides being carried by the exhaust gas in an SCR catalyst arranged downstream. Instead of ammonia, urea or an aqueous urea solution may also be injected into the exhaust gas stream. Ammonia and water will then form from the urea-water solution by a hydrolysis reaction. Furthermore, a fuel or another suitable reducing agent may be injected into the exhaust gas stream upstream of an NOx storage catalyst in order to regenerate the NOx storage catalyst.
To improve or make possible the mode of action of the educt injected in the liquid form into the exhaust gas line, extensive evaporation is just as desirable as a thorough mixing with the exhaust gas in order to thus obtain the most homogeneous exhaust gas-educt mixture possible. The exhaust system may be equipped for this with a mixing and/or evaporating device arranged in the exhaust gas line downstream of the injection means.
Depending on the injection means used, the educt may be introduced in the form of a liquid jet, which flares up in a conical shape. Low exhaust gas temperatures and low flow velocities prevail at low engine loads and exhaust gas temperatures. The liquid jet can subsequently impact on a corresponding structure of the mixing and/or evaporating device. Depending on the design of the mixing and/or evaporating device, the liquid jet may pass through the particular structure of the mixing and/or evaporating device at least partially and then reach in the liquid form an exhaust gas treatment means, at which the injected liquid shall only arrive in the form of the most homogeneous gas mixture possible. The consequence is a reduced mode of action as well the risk of damage.
The present invention pertains to the object of providing an improved embodiment for a mixing and/or evaporating device or an exhaust system equipped therewith or for a corresponding manufacturing process, which improved embodiment is characterized especially by the possibility of manufacture at a low cost. In addition, improved evaporating action may be desirable.
The present invention is based on the general idea of manufacturing the mixing and/or evaporating device from a single sheet metal body only, on which a tubular body and blades projecting therefrom radially inwardly are formed for this purpose. The mixing and/or evaporating device can be manufactured at a comparatively low cost as a result. The blades are arranged and designed according to the present invention specifically in such a way that they have an angle of incidence in relation to the axial direction of the tubular body. The resistance to flow is increased hereby in the area of the blades and a twist is generated. The twist in the exhaust gas stream generates swirling, which supports the evaporation of the possibly liquid educt, on the one hand, and improves the homogenization of the mixture, on the other hand.
The blades may be advantageously arranged and designed such that they overlap in the circumferential direction, doing so such that a coaxially arranged composite surface, which blocks a straight line path in the axial direction, is formed. Breakthrough of liquid droplets through the mixer structure is avoided due to the formation of such an axial path blocking surface. The droplets impact on the blades in the surface and can evaporate more easily as a result.
According to a variant, the blades may be designed and arranged such that the surface formed by the overlapping of the blades is an annular surface, which encloses a central core area. It becomes possible as a result to design the core area and the annular surface differently from the fluidic point of view. In particular, it is possible to design and arrange the blades such that a lower resistance to flow will become established in the core area than in the area of the annular surface. The pressure can be lowered as a result in the core area, which can be utilized to accelerate the flow of the exhaust gas in the center. The increased velocity of flow in the center facilitates the evaporation of the liquid jet. It is especially advantageous now to direct the liquid jet such that it will reach the blades radially outside the central core area.
To reduce the resistance to flow in the core area compared to the area of the annular surface, provisions may be made to design the core area as a central passage opening, which is free or open axially. As an alternative, the core area may also be made essentially a straight line axial area block in order to make it possible to effectively avoid breakthrough of liquid droplets here as well. An axial path blocking core area with reduced resistance to flow compared to the annular surface can be obtained, for example, such that not all but only some of the blades extend up into the core area and/or that the blades overlap less extensively in the core area than in the annular surface. In particular, provisions may be made for the blades, which extend up into the core area, not to overlap in the core area in the circumferential direction but to be arranged only next to each other.
Other important features and advantages of the present invention appear from the from the drawings and from the corresponding description of the figures on the basis of the drawings. It is apparent that the above-mentioned features, which will still be explained below, are applicable not only in the particular combination indicated, but in other combinations or alone as well, without going beyond the scope of the present invention.
Preferred exemplary embodiments of the present invention are shown in the drawings and will be explained in more detail below, identical reference numbers designating identical or similar or functionally identical components. The various features of novelty which characterize the invention are pointed out with particularity in the claims annexed to and forming a part of this disclosure. For a better understanding of the invention, its operating advantages and specific objects attained by its uses, reference is made to the accompanying drawings and descriptive matter in which preferred embodiments of the invention are illustrated.
In the drawings:
a is a view as in
b is a view as in
a is a view as in
b is a view as in
a is a view of a sheet metal body in one of different states within the framework of the manufacture of a mixing and/or evaporating device according to
b is a view of a sheet metal body in another of different states within the framework of the manufacture of a mixing and/or evaporating device according to
c is a view of a sheet metal body in another of different states within the framework of the manufacture of a mixing and/or evaporating device according to
d is a view of a sheet metal body in another of different states within the framework of the manufacture of a mixing and/or evaporating device according to
e is a view of a sheet metal body in another of different states within the framework of the manufacture of a mixing and/or evaporating device according to
f is a view of a sheet metal body in another of different states within the framework of the manufacture of a mixing and/or evaporating device according to
g is a view of a sheet metal body in another of different stats within the framework of the manufacture of a mixing and/or evaporating device according to
a is a view of a sheet metal body in one of different manufacturing steps of a mixing and/or evaporating device according to
b is a view of a sheet metal body in another of different manufacturing steps of a mixing and/or evaporating device according to
c is a view of a sheet metal body in another of different manufacturing steps of a mixing and/or evaporating device according to
d is a view of a sheet metal body in another of different manufacturing steps of a mixing and/or evaporating device according to
Referring to the drawings in particular,
According to
To make it possible to evaporate the liquid educt injected as rapidly and as completely as possible in the exhaust gas and in order to nix the evaporated educt as homogeneously as possible with the exhaust gas, the exhaust system 3 is equipped with a mixing and/or evaporating device 7, which is arranged in the exhaust gas line 4 downstream of the injection means 6 and preferably upstream of or directly at or in the exhaust gas treatment means 5 located adjacent to the injection means 6.
Preferred embodiments of the mixing and/or evaporating device 7, which will hereinafter also be called device 7 for short, will be explained in more detail below with reference to
Corresponding to
It is especially advantageous now that the particular tubular body 8 is manufactured, together with all blades 9, from a single sheet metal body 11, doing so by shaping corresponding areas of this sheet metal body 11. The particular device 7 is consequently a sheet metal shaped body manufactured from one piece.
In the preferred embodiments shown here, the blades 9 are designed and arranged such that they mutually overlap in the circumferential direction, doing so such that a composite surface 12 is formed, which is axial path blocking in the axial direction. This axial path blocking surface 12 may be shaped, in principle, as a circular surface due to a corresponding design and arrangement of the blades 9. Breakthrough of droplets through the device 7 can be avoided as a result especially effectively. As an alternative, the blades 9 may also be arranged and designed such that surface 12 is, as in the embodiments being shown here, an annular surface, which will hereinafter likewise be designated by 12. The annular surface 12 encloses a central core area 10. Due to a specific design, i.e., shaping and arrangement of the blades 9, the fluidic properties of the device 7 can now be made different in this core area 10 as well as in the area of the annular surface 12. Preferred in this connection are the embodiments being shown here, in which the blades 9 are designed and arranged such that a lower value becomes established for the resistance to flow of the device 7 in the core area 10 than in the area of the annular surface 12. The pressure decreases as a result in the core area 10, which leads to an acceleration of the flow. The increased flow velocity supports the evaporation, on the one hand, and mixture formation, on the other hand.
In the embodiments according to
Contrary to this, the core area 10 can also be made extensively axial path blocking in the axial direction in the embodiment shown in
In the preferred example being shown, exactly two blades 9′ are made radially longer, without limitation of the general nature, than the other blades 9. The free blade ends of these blades 9′ are extended in the radial direction by extensions 22 compared to the free ends of the other blades 9. These extensions 22, which are made integrally in one piece with the respective blades 9′, may project radially over a center of the surface 12 or of the device 7, which said center is not shown here. This means that the radial length of the particular blade 9′ is greater than the radius of the regular cylindrical tubular body 8. At any rate, these blades 9′ with the extensions 22 protrude into the core area 10, whereas all other blades 9 with their free ends end each at the core area 10.
The two blades 9′ provided with the extensions 22 are arranged diametrically opposite each other at the tubular body 8. The extensions 22 may be oriented such that they are rotationally symmetrical in respect to the center of the tubular body 8. The two blades 9′ may slightly overlap in the area of their extensions 22 in the circumferential direction, but they are preferably free from overlapping in the circumferential direction, i.e., they are arranged next to each other. The radially longer blades 9′ are especially twisted uniformly up to the extensions 22, so that the twisting of this blade 9′ is smallest in the core area, as a result of which the resistance to flow through the blades 9′ is lowest in the center.
The blades 9 are designed and arranged in the embodiments shown in
To design such an axial path blocking annular surface 12, the blades 9 are designed radially outwardly at a transition 13 to the tubular body 8 in the embodiment according to
This mode of construction with the axially free gaps 14 can be preferably obtained by the blades 9 being located radially on the outside at the transition 13 to the tubular body 8 with their respective cross-sectional profile in a plane that is sloped relative to a plane extending at right angles to the axial direction. This slope may be, for example, between 20° and 70°. This slope is preferably about 45° in the example being shown.
In the embodiments according to
To increase the fatigue strength of the mixing and/or evaporating device 7, the individual blades 9 adjacent to each other in the circumferential direction may border on each other radially outside at the transition 13 to the tubular body 8 via a rounded opening 15 each. These rounded openings 15 can be better recognized, e.g., in
Embodiments in which the blades 9, 9′ are designed and arranged such that they do not touch each other are especially advantageous. Advantageous here is a variant in which the blades 9, 9′ do not touch each other even if the device 7 has been heated to the operating temperature, which may be comparatively high in an exhaust system 3. Damage and disturbing noise generation within the device 7 can be avoided due to this contact-free mode of construction.
A preferred process for manufacturing the mixing and/or evaporating device 7 will be explained in more detail below on the basis of
Corresponding to
The rounded openings 15 can subsequently be optionally prepared in the sheet metal strip 16 according to
A plurality of cross strips 19, which are arranged next to each other in the longitudinal direction 18 of the sheet metal strip 16 and which are separated from one another by the cuts 17, are formed by the cuts 17 on the sheet metal strip 16. These cross strips 19 will then later form the blades 9, which are already separated here from each other by the cuts 17. To form the embodiment shown in
According to
According to
According to
To make it possible to manufacture the embodiment shown in
According to
In this embodiment, the blades 9 already have an angle of incidence in relation to the axial direction of the tubular body 8 after bending. Furthermore, the course of the angle of incidence can still be changed along the respective blade 9, for example, by twisting or by changing the angle of incidence in increments, for example, by folding at least one predetermined area within the blades 9. The sheet metal strip 16 thus formed is then wound up as well in order to form the tubular body 8.
To manufacture the embodiment shown in
In addition, it can be determined from the views in
The injection means 6 and the mixing and/or evaporating device 7 are preferably coordinated with one another in the exhaust system 3 shown in
While specific embodiments of the invention have been shown and described in detail to illustrate the application of the principles of the invention, it will be understood that the invention may be embodied otherwise without departing from such principles.
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