This application claims priority of German patent application no. 10 2022 133 786.3, filed Dec. 19, 2022, the entire content of which is incorporated herein by reference.
The present disclosure relates to a mixing section for an exhaust system of an internal combustion engine, for intermixing exhaust gas and reagent.
With a view to lessening the pollutant content in exhaust gas emitted by an internal combustion engine, it is known to inject a reagent, for instance a urea/water solution, into the exhaust gas. In a catalytically active exhaust-gas treatment arrangement, for instance in an SCR catalytic converter, a catalytic reaction resulting in the lessening of the pollutant content, for instance a selective catalytic reduction, is carried out using the reagent.
It is an object of the present disclosure to provide a mixing section for an exhaust system of an internal combustion engine, with which, with a small construction-space requirement, an efficient mixing of exhaust gas and of reagent injected into the mixing section is obtained.
In accordance with the disclosure, this object is, for example, achieved via a mixing section for an exhaust system of an internal combustion engine, for intermixing exhaust gas and reagent, including:
By virtue of the wetting of the reagent-receiving elements arranged in the mixing chamber with the reagent injected into the mixing chamber, a comparatively large surface is utilized in order to evaporate the reagent, generally injected in liquid form as a spray mist with a large number of reagent droplets, and to mix it with the exhaust gas vortexed in the mixing chamber.
For a structurally simple configuration, at least one reagent-receiving element, preferentially each reagent-receiving element, may have been formed in plate-like manner and may exhibit a substantially flat reagent-receiving area.
In order to avoid a mutual shielding of the reagent-receiving elements, it is proposed that a plurality of passage openings have been formed in at least one reagent-receiving element, preferentially in each reagent-receiving element.
An efficient wetting of the reagent-receiving areas can be obtained by the reagent-receiving area in the case of at least one reagent-receiving element, preferentially in the case of each reagent-receiving element, being oriented substantially orthogonally to the main dispensing direction or/and being oriented substantially parallel to a center axis of at least one exhaust-gas inlet opening. Furthermore, there may be provision that at least two reagent-receiving areas, preferentially all the reagent-receiving areas, are substantially parallel to one another.
A mutual shielding of the reagent-receiving elements against a wetting with the reagent injected into the mixing chamber can be further prevented if in the case of at least two reagent-receiving elements directly adjacent to one another, preferentially in the case of all the reagent-receiving elements directly adjacent to one another, the reagent-receiving area of the reagent-receiving element positioned closer to the reagent-dispensing unit is smaller than the reagent-receiving area of the reagent-receiving element positioned further away from the reagent-dispensing unit.
For the purpose of obtaining a compact style of construction, it is proposed that in the case of at least two reagent-receiving elements directly adjacent to one another, preferentially in the case of all the reagent-receiving elements directly adjacent to one another, the reagent-receiving area of the reagent-receiving element positioned closer to the reagent-dispensing unit is substantially completely overlapped at right angles to the main dispensing direction by the reagent-receiving area of the reagent-receiving element positioned further away from the reagent-dispensing unit.
A reliable wetting of reagent-receiving elements positioned further away from the reagent-dispensing unit can be guaranteed if a size of the reagent-receiving areas of the reagent-receiving elements increases in the main dispensing direction.
For a uniform wetting of the entire reagent-receiving arrangement, it is proposed that a dispensing location of the reagent-dispensing unit in at least one direction at right angles to the main dispensing direction is positioned substantially centrally with respect to an outer peripheral contour of the reagent-receiving arrangement.
For this purpose, there may be provision that the outer peripheral contour of the reagent-receiving arrangement corresponds substantially to an outer peripheral contour of the reagent-receiving element having the largest reagent-receiving area.
At least one exhaust-gas inlet opening, preferentially each exhaust-gas inlet opening, may be elongated in the direction of a longitudinal axis thereof preferentially substantially parallel to the main dispensing direction, as a result of which an excessive throttling of the stream of exhaust gas is avoided. In this connection, it is particularly advantageous if at least two exhaust-gas inlet openings elongated in the direction of a respective longitudinal axis thereof with longitudinal axes substantially parallel to one another and overlapping one another in the direction of the longitudinal axes thereof at least partially, preferentially substantially completely, have been provided in the housing base.
For a stable mounting of the reagent-receiving elements, the latter may be supported on the housing base between the at least two exhaust-gas inlet openings.
If at least one reagent-receiving element, preferentially each reagent-receiving element, extends at least partially across at least one exhaust-gas inlet opening at right angles to the main dispensing direction, an efficient interaction of a reagent-receiving element positioned in such a manner with the stream of exhaust gas is guaranteed, in particular also for the purpose of heating the reagent-receiving element. In this connection, it is particularly advantageous if all the reagent-receiving elements at right angles to the main dispensing direction extend at least partially across the same exhaust-gas inlet opening.
For the purpose of obtaining a turbulence, assisting the intermixing, of the exhaust gas introduced into the mixing chamber, the mixing-section housing may exhibit an exhaust-gas-deflecting wall, situated opposite the housing base, with a concave inner deflecting surface facing toward the mixing chamber.
If the inner deflecting surface exhibits a vertex region with maximum spacing from the housing base, and a substantially vertical projection of the vertex region onto the housing base is situated between two exhaust-gas inlet openings, two exhaust-gas vortices oriented contrary to one another are generated in the mixing chamber, as a result of which the intermixing of exhaust gas with reagent injected into the mixing chamber, or evaporating from the reagent-receiving areas, is further assisted.
In order to be able to utilize the turbulence of exhaust gas in the mixing chamber efficiently for the purpose of intermixing with reagent injected into the mixing chamber, it is further proposed that the vertex region is elongated in the direction of the longitudinal axis of the at least one exhaust-gas inlet opening or/and in the main dispensing direction.
For the purpose of dispensing the mixture of exhaust gas and reagent generated in the mixing section, the mixing-section housing may exhibit an exhaust-gas outlet opening, a main inflow direction of exhaust gas flowing through the at least one exhaust-gas inlet opening being substantially orthogonal to a main outflow direction of exhaust gas flowing through the exhaust-gas outlet opening.
The disclosure further relates to an exhaust system for an internal combustion engine, including a mixing section constructed in accordance with the disclosure.
At least one exhaust-gas treatment arrangement, preferentially including an oxidation catalytic converter or/and a particle filter, may have been arranged upstream of the mixing section. For the purpose of causing the mixture of exhaust gas and reagent to react, at least one exhaust-gas treatment arrangement, preferentially including an SCR catalytic converter, may have been arranged downstream of the mixing section.
The invention will now be described with reference to the drawings wherein:
The mixing section 16 includes a mixing-section housing denoted generally by 22. The mixing-section housing 22 includes a housing part 24 formed substantially in dome-like manner and provided, for instance, as a sheet-metal formed part in one piece or in multiple pieces. The housing part 24 may have been linked in its upstream end region 26 to the upstream exhaust-gas treatment arrangement 12.
The mixing-section housing 22 further includes a housing base 28, formed substantially in plate-like manner and likewise provided, for instance, as a sheet-metal formed part. The housing base 28, represented in more detailed manner in
In the embodiment represented, two exhaust-gas inlet openings 341, 342 have been formed in the housing base 28. Center axes M1, M2 of the exhaust-gas inlet openings 341, 342 are oriented substantially orthogonally to the substantially flat surface 32 of the housing base 28. The exhaust gas A entering the mixing chamber 20 from the upstream exhaust-gas treatment arrangement 12 flows through the exhaust-gas inlet openings 341, 342 substantially in a respective main inflow direction E1, E2, these directions being approximately parallel to the respective center axis M1, M2 of the opening.
The two exhaust-gas inlet openings 341, 342 are arranged in the housing base 28 in such a manner that the longitudinal axes L1, L2 thereof are substantially orthogonal to the respective center axes M1, M2 thereof and are substantially parallel to one another and preferentially also to the main dispensing direction H. Furthermore, the exhaust-gas inlet openings 341, 342 are positioned in such a way that they overlap one another substantially completely in the direction of their longitudinal axes L1, L2, which may mean that the two exhaust-gas inlet openings 341, 342 have substantially the same length in the direction of their respective longitudinal axes L1, L2 and also preferentially have the same width at right angles to the respective longitudinal axis L1, L2.
In
The housing part 24 enclosing, together with the housing base 28, the mixing chamber 20 is shaped in dome-like manner, in particular in its region situated opposite the housing base 28, and provides a deflecting wall 38 with an inner deflecting surface 40 facing toward the mixing chamber 20 and concave with respect to the mixing chamber 20. By reason of the dome-like shape, the inner deflecting surface 40 exhibits a vertex region S in which the inner deflecting surface 40 has the maximum spacing from the housing base 28, or from the substantially flat surface 32 thereof. A vertical projection of the vertex region S onto the housing base 28, indicated by a projection arrow P1 in
By virtue of this structure of the housing part 24 in the region of its deflecting wall 38, the exhaust gas A introduced into the mixing chamber 20 through the exhaust-gas inlet openings 341, 342 in the respective main inflow direction E1, E2 is deflected in such a way that two exhaust-gas vortices W1, W2 oriented contrary to one another arise. In the case of the aforementioned linearly extended shape of the vertex region S, these exhaust-gas vortices W1, W2 may also, in principle, have a roller-like structure extended in this direction by reason of the elongated shape of the exhaust-gas inlet openings 341, 342 in the same direction.
A reagent-receiving arrangement, denoted generally by 42, is arranged in the mixing chamber 20. In the example represented, the reagent-receiving arrangement 42 includes three reagent-receiving elements 441, 442, 443 formed substantially in plate-like manner, which take the form, for instance, of sheet-metal formed parts. The reagent-receiving elements 441, 442, 443 formed in plate-like manner may, for instance, have been fixed in a region between the two exhaust-gas inlet openings 341, 342 by materially closed linkage to the housing base 28.
Each reagent-receiving element 441, 442, 443 exhibits a substantially flat—that is, non-curved—reagent-receiving area 461, 462, 463 oriented facing toward the reagent-dispensing unit 18. The reagent-receiving elements 441, 442, 443 are arranged in the mixing chamber 20 in such a way that the substantially flat, non-curved reagent-receiving areas 461, 462, 463 thereof are oriented substantially orthogonally to the main dispensing direction H and are oriented substantially parallel to the main inflow direction E1, E2 which is present at a respective exhaust-gas inlet opening 341, 342, and also to one another. Consequently the reagent-receiving elements 441, 442, 443 do not substantially impede the inflow of exhaust gas A into the mixing chamber 20 but provide a maximum receiving interaction with the reagent R injected into the mixing chamber 20.
The reagent-receiving elements 441, 442, 443, arranged succeeding one another in the main dispensing direction H, have been configured in such a way that the size of the reagent-receiving area 461, 462, 463 respectively provided thereon increases in the direction away from the reagent-dispensing unit 18—that is, substantially also in the main dispensing direction H. Reagent-receiving element 441 positioned closest to the reagent-dispensing unit 18 exhibits the smallest reagent-receiving area 461, whereas reagent-receiving element 443 situated furthest away from the reagent-dispensing unit 18 provides the largest reagent-receiving area 463.
As can be discerned in particular in
In order to obtain an efficient wetting of all the reagent-receiving elements 441, 442, 443 with the reagent R, the reagent-dispensing unit 18 is positioned or oriented in such a way that a dispensing location O at which the reagent R is dispensed in the main dispensing direction H by the reagent-dispensing unit 18 is situated substantially directly opposite the center Z of the outer peripheral contour of the reagent-receiving arrangement 42 when viewed in the main dispensing direction H, this being illustrated in
In order to avoid, as far as possible, a mutual shielding of the reagent-dispensing elements 441, 442, 443 succeeding one another in the main dispensing direction H, a large number of passage openings 481, 482, 483 may have been provided in each of these elements. Some of the reagent R which is to flow onto a respective reagent-receiving element 461, 462, 463 is consequently not received on these elements but in the region of the passage openings 481, 482, 483 flows through the latter and can consequently, on the one hand, wet reagent-receiving elements 442, 443 then following in the main dispensing direction H or can mix downstream of the last reagent-receiving element 443 with the exhaust gas A flowing in this volume region in the mixing chamber 20.
In particular in
The mixture G of exhaust gas A and reagent R formed in the mixing chamber 20 leaves the mixing-section housing 22 in the region of an exhaust-gas outlet opening 50 substantially in a main outflow direction S which is oriented approximately orthogonally to the main inflow directions E1, E2. This results in a compact structure of the mixing section 16, or of the entire exhaust system 10, and, by reason of the deflection of the flow by approximately 90° arising in the region of the mixing chamber 20 and superimposed on the turbulence, results in a further mixing of exhaust gas A and reagent R already taken up in the exhaust gas. Consequently it is guaranteed that an exhaust gas A that has been intermixed substantially uniformly with reagent R flows into the downstream exhaust-gas treatment arrangement 14, for instance through a transition housing 52, and consequently can enter into interaction within the arrangement, distributed over the cross-section thereof, in substantially uniform manner with the catalytically active material provided therein for the purpose of implementing the stipulated exhaust-gas cleanup function.
It should be pointed out that various variations can be undertaken in respect of the mixing section presented in the foregoing on the basis of an embodiment. For instance, more than the three reagent-receiving elements presented might have been provided. In the sequence of reagent-receiving elements, two reagent-receiving elements directly adjacent to one another having equally large reagent-receiving areas, for instance, might also have been formed. It should be pointed out that with respect to the orientation, elucidated in the foregoing, of various components or configuration aspects—for instance, orthogonal or parallel to one another—the respective orientations may deviate slightly from an exact parallel or orthogonal orientation in the given case, without this resulting in an impairment of the intermixing of exhaust gas and reagent to be brought about by the interaction of the various system regions.
It is understood that the foregoing description is that of the preferred embodiments of the invention and that various changes and modifications may be made thereto without departing from the spirit and scope of the invention as defined in the appended claims.
Number | Date | Country | Kind |
---|---|---|---|
10 2022 133 786.3 | Dec 2022 | DE | national |