The invention relates to a device for metering liquid pollutant-reducing media into an exhaust gas duct of the exhaust gas line of an internal combustion engine, a method for metering liquid, pollutant-reducing media into an exhaust gas duct of the exhaust gas line of an internal combustion engine and a static mixer.
The generic DE 10 2004 048 075 A1 discloses a device and a method for metering liquid, pollutant-reducing media into an exhaust gas duct of the exhaust gas line of an internal combustion engine in which by means of a metering device located in an exhaust gas duct the liquid is injected in the form of one or more string-shaped liquid jets, and these jets are to be directed at a baffle plate or baffle body in order to achieve the corresponding liquid distribution. Other details in this respect are not disclosed. Alternatively, it is provided that the liquid be injected by means of a spray nozzle, the so-called injection site being located in the curve region of an exhaust gas duct. In this version there is no baffle plate or baffle body.
A similar structure is also known from DE 197 41 199 C2 in which the reducing agent is injected within the pipe elbow of an exhaust gas duct. Upstream and downstream from the elbow is one static mixer at a time which is made as an expanded grating with a number of meshes formed by intermediate bridges. With this static mixer the exhaust gas flow in the exhaust gas duct is to be made uniform.
Furthermore U.S. Pat. No. 6,905,658 B2 discloses a structure in which the exhaust gas duct in front of the inlet to the actual catalytic converter is divided into a plurality of individual flow channels, each of these flow channels being assigned its own metering means for the reducing agent.
Conversely, the object of this invention is to make available a device and a method for metering liquid, pollutant-reducing media, such as, for example, ammonia or urea, into an exhaust gas duct of the exhaust gas line of an internal combustion engine as well as a static mixer by means of which extremely fine distribution or atomization of the liquid, pollutant-reducing media to be metered becomes easily and reliably possible.
According to a first aspect of this invention, the baffle body is formed by a static mixer which has a plurality of preferably single-blade guide vane plates which project away from the mixer plane at a given angle and which are aligned such that the metered liquid strikes the plane of the guide vane plates essentially perpendicularly.
With this execution of a static mixer an especially effective, extremely fine distribution of the metered liquid which can be, for example, ammonia or urea is achieved, since the perpendicular incidence of the liquid, preferably of liquid droplets, leads to the desired fine atomization of the liquid. This effective fine atomization of the liquid droplets which have injected, for example, by means of a spray nozzle in conjunction with the plurality of guide vane plates enables an especially uniform distribution of the metered reducing agent in the exhaust gas flow; this again then enables especially effective reduction of pollutants in the catalytic converter, especially within the scope of so-called selective catalytic reduction (SCR) in which the NOx conversion takes place in a lean atmosphere by way of specially made catalytic converters. That is, that in conjunction with the solution according to the invention the liquid droplets which have already been injected anyway by means of a spray nozzle, for example, can be easily and reliably atomized again for extremely fine distribution in the exhaust gas flow. For metering the reducing agent, durable, heavy-duty spray nozzles can also be used which have a nozzle head which makes available a larger droplet size and therefore does not clog as easily as would being the case in special nozzles which enable extremely fine atomization with the corresponding special nozzle heads.
Fundamentally the metering of liquid droplets is preferred in order to be able to undertake a first extremely fine distribution within the framework of metering by way of the metering means. But it is also fundamentally possible not to meter the liquid drop by drop, but in the form of one or more liquid jets which can them likewise be atomized upon perpendicular impact on the planes of the guide vane plate.
According to one especially preferred configuration of the invention it is furthermore provided that the guide vane plates of the static mixer are essentially aligned the same, i.e., essentially have the same extension direction, by which it can be easily ensured that the liquid droplets deflected or entrained by the exhaust gas flow in any region of the static mixer can perpendicularly strike the plane of the guide vane plate of the static mixer in order to achieve the desired atomization of the injected liquid droplets.
According to another preferred configuration of the invention it is further provided that the guide vane plates all are made identically and/or are tilted against the plane of the mixer with an identical tilt angle. This static mixer can be easily manufactured and at any site of the static mixer delivers the same atomization conditions. Preferably the tilt angle of the guide vane plate against the mixer plane is in the range between 20° to 80°, preferably between 40° and 60°.
The guide vane plates according to another preferred configuration relative to the mixer plane are arranged in several rows of guide vanes, the individual rows of guide vanes and/or the individual guide vane plates of a row of guide vanes having a given, preferably identical distance from one another. Thus a reliable static mixer which is altogether very simple to produce with single-blade vanes is made available.
The mixer itself, according to another preferred configuration of the invention, can have a support grating which lies in the mixer plane, consisting of grating braces aligned at a right angle to one another, the support grating having a plurality of essentially rectangular, in particular square grating openings which are separated from one another by the grating braces and which lie next to one another. The guide vanes themselves on the opening side are coupled to a grating brace region which forms the opening side wall and project away from it in single vanes or scale-like and/or blade-like, tilted in a given direction. In particular, here the guide vane plate is formed by an essentially planar and/or rectangle-shaped vane plate, by which perpendicular impact of the liquid droplets or liquid jet can be achieved especially easily. But fundamentally slightly arched configurations of the individual guide vane plates are also possible; this, however, in turn means increased production costs. The static mixer itself can be produced from a metal and/or plastic material, and the guide vane plates can be coupled on the support grating, for example, by welding or the like.
The mixer itself preferably has an outer ring which is closed in a ring shape and in which the support grating is formed. This outer ring is connected at least in certain sections to one wall of the exhaust gas duct, preferably in a flat contact connection. This contact connection is produced, for example, by welding.
According to another aspect according to the invention, the metering means is located in or on the exhaust gas duct such that the liquid metered by this metering means, especially the liquid droplets injected by a metering means which is designed as a spray nozzle, are deflected by the exhaust gas flow such that these, for example, liquid droplets perpendicularly strike the plane of the plate of guide vanes. For this purpose, the metering means is preferably located in the region of the pipe elbow, preferably in or on the outer curved wall region of this pipe elbow of the exhaust gas duct so that the liquid is injected or sprayed in the direction to the plane of the static mixer and/or the liquid droplets have a ballistic, i.e. convexly curved flight path. In this way outstanding atomization results are achieved. The liquid or liquid droplets are metered in this connection in a controlled manner by way of a control means.
According to one especially preferred configuration, the metering means is located in a targeted manner in conjunction with the static mixer such that a ballistic flight path is impressed onto the liquid jet or liquid droplets, especially by deflection by means of the exhaust gas flow such that the liquid jets or liquid droplets strike the guide vane plates perpendicularly in their “sinking flight phase”, by which especially effective extremely fine atomization is enabled.
A specific structure is especially preferred in which the guide vane plates viewed in the direction of the vertical axis of the vehicle project to the top away from the mixer plane since here then the guide vane plates in the optimum manner have a vertical impact surface for the liquid jets or liquid droplets which have a natural flight path.
As can be taken from the schematic in
As is likewise schematically shown in
This static mixer 12 is shown in detail in
In the outer ring 14 a support grating 15 of grating braces 16, 17 which are aligned at a right angle to one another and which form essentially square grating openings 18 is held. As can be taken especially from
The individual guide vane plates 11 which are each made single-blade here, by an essentially flat, rectangular vane plate are coupled in the region of the side wall of the grating openings 18 which is formed by the grating braces 16, 17, and project away from there tilted in a given direction. The tilt angle is between 20° to 80°, at most preferably between 40° to 60°, relative to the mixer plane.
As can furthermore be taken from
The guide vane plates 11 in the projected top view of
Number | Date | Country | Kind |
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10 2007 020 812.1 | May 2007 | DE | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP08/01947 | 5/12/2008 | WO | 00 | 10/29/2009 |