Dosing and mixing arrangement for use in exhaust aftertreatment
15 claims: 2 independent, 13 dependent
- 1A mixing tube arrangement for swirling exhaust gases, the mixing tube arrangement comprising:a tube body having a longitudinal axis extending along an interior passage from a first end of the tube body to a second end of the tube body, the tube body defining a slotted region and a non-slotted region, the slotted region defining a plurality of slots, the slotted region extending over a first circumferential distance of the tube body and the non-slotted region extending over a second circumferential distance of the tube body, the second circumferential distance being less than the first circumferential distance;and a plurality of louvers disposed at the slots, characterized in that the slotted region extends along about 210° to about 330°of a circumference of the tube body.
- 10A dosing and mixing arrangement comprising:a housing defining an inlet having an inlet axis, a mixing region, and an outlet having an outlet axis, the outlet axis being generally orthogonal to the inlet axis;a mixing tube arrangement according to any one of claims 1-9 disposed within the mixing region of the housing.
Independent claims2
44 paragraphs in 5 sections, as filed
CROSS-REFERENCE TO RELATED APPLICATION(S)
0001This application is being filed on September 12, 2014, as a PCT International Patent application and claims priority to <patcit id="pcit0001" dnum="US61877749A" dnum-type="L"><text>U.S. Patent Application Serial No. 61/877,749 filed on September 13, 2013</text></patcit>.
BACKGROUND
0002Vehicles equipped with internal combustion engines (e.g., diesel engines) typically include exhaust systems that have aftertreatment components such as selective catalytic reduction (SCR) catalyst devices, lean NOx catalyst devices, or lean NOx trap devices to reduce the amount of undesirable gases, such as nitrogen oxides (NOx) in the exhaust. In order for these types of aftertreatment devices to work properly, a doser injects reactants, such as urea, ammonia, or hydrocarbons, into the exhaust gas. As the exhaust gas and reactants flow through the aftertreatment device, the exhaust gas and reactants convert the undesirable gases, such as NOx, into more acceptable gases, such as nitrogen and water. However, the efficiency of the aftertreatment system depends upon how evenly the reactants are mixed with the exhaust gases. Therefore, there is a need for a flow device that provides a uniform mixture of exhaust gases and reactants.
0003SCR exhaust treatment devices focus on the reduction of nitrogen oxides. In SCR systems, a reductant (e.g., aqueous urea solution) is dosed into the exhaust stream. The reductant reacts with nitrogen oxides while passing through an SCR substrate to reduce the nitrogen oxides to nitrogen and water. When aqueous urea is used as a reductant, the aqueous urea is converted to ammonia which in turn reacts with the nitrogen oxides to covert the nitrogen oxides to nitrogen and water. Dosing, mixing and evaporation of aqueous urea solution can be challenging because the urea and by-products from the reaction of urea to ammonia can form deposits on the surfaces of the aftertreatment devices. Such deposits can accumulate over time and partially block or otherwise disturb effective exhaust flow through the aftertreatment device.
0004<patcit id="pcit0002" dnum="EP2128398A1"><text>EP 2 128 398 A1</text></patcit> discloses a mixing tube arrangement for swirling exhaust gases according to the preamble of claim 1.
SUMMARY
0005The present invention relates to a mixing tube arrangement for swirling exhaust gases as defined in appended claim 1. An aspect of the present disclosure relates to a method for dosing and mixing exhaust gas in exhaust aftertreatment. Another aspect of the present disclosure relates to a dosing and mixing unit for use in exhaust aftertreatment. More specifically, the present disclosure relates to a dosing and mixing unit including a mixing tube configured to direct exhaust gas flow to flow around and through the mixing tube to effectively mix and dose exhaust gas within a relatively small area.
0006In accordance with some aspects, the mixing tube includes a slotted region and a non-slotted region. In examples, the slotted region extends over a majority of a circumference of the mixing tube. In examples, the slotted region extends over a majority of an axial length of the mixing tube. In examples, a circumferential width of the non-slotted region is substantially larger than a circumferential width of a gap between slots of the slotted region.
0007In accordance with some aspects, the mixing tube includes a louvered region and a non-louvered region. The louvered region extends over a majority of a circumference of the mixing tube. In examples, the louvered region extends over a majority of an axial length of the mixing tube. In examples, a circumferential width of the non-slotted region is substantially larger than a circumferential width of a gap between louvers of the louvered region.
0008In accordance with some aspects, the mixing tube is offset within a mixing region of a housing. For example, the mixing tube can be located closer to one wall of the housing than to an opposite wall of the housing.
0009A variety of additional aspects will be set forth in the description that follows. These aspects can relate to individual features and to combinations of features. It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the broad concepts upon which the embodiments disclosed herein are based.
DRAWINGS
0010The accompanying drawings, which are incorporated in and constitute a part of the description, illustrate several aspects of the present disclosure. A brief description of the drawings is as follows: <ul id="ul0001" list-style="none" compact="compact"><li><figref idref="f0001">FIG. 1</figref> is a schematic representation of a first exhaust treatment system incorporating a doser and mixing unit in accordance with the principles of the present disclosure;</li><li><figref idref="f0002">FIG. 2</figref> is a schematic representation of a second exhaust treatment system incorporating a doser and mixing unit in accordance with the principles of the present disclosure;</li><li><figref idref="f0003">FIG. 3</figref> is a schematic representation of a third exhaust treatment system incorporating a doser and mixing unit in accordance with the principles of the present disclosure;</li><li><figref idref="f0004">FIG. 4</figref> is a perspective view of an example doser and mixing unit configured in accordance with the principles of the present disclosure;</li><li><figref idref="f0005">FIG. 5</figref> is a cross-sectional view of the doser and mixing unit of <figref idref="f0004">FIG. 4</figref> taken along the plane 5 of <figref idref="f0004">FIG. 4</figref>;</li><li><figref idref="f0006">FIG. 6</figref> is a cross-sectional view of the doser and mixing unit of <figref idref="f0004">FIG. 4</figref> taken along the housing axis C shown in <figref idref="f0005">FIG. 5</figref>;</li><li><figref idref="f0007">FIG. 7</figref> is a perspective view of an example mixing tube arrangement suitable for use with the doser and mixing unit of <figref idref="f0004">FIG. 4</figref>;</li><li><figref idref="f0008">FIG. 8</figref> is a side elevational view of the mixing tube arrangement of <figref idref="f0007">FIG. 7</figref>; and</li><li><figref idref="f0009">FIG. 9</figref> is an end view of the mixing tube arrangement of <figref idref="f0007">FIG. 7</figref>.</li></ul>
DETAILED DESCRIPTION
0011Reference will now be made in detail to the exemplary aspects of the present disclosure that are illustrated in the accompanying drawings. Wherever possible, the same reference numbers will be used throughout the drawings to refer to the same or like structure.
0012<figref idref="f0001 f0002 f0003">FIGS. 1-3</figref> illustrate various exhaust flow treatment systems including an internal combustion engine 201 and a dosing and mixing unit 207. <figref idref="f0001">FIG. 1</figref> shows a first treatment system 200 in which a pipe 202 carries exhaust from the engine 201 to the dosing and mixing unit 207, where reactant (e.g., aqueous urea) is injected (at 206) into the exhaust stream and mixed with the exhaust stream. A pipe 208 carries the exhaust stream containing the reactant from the dosing and mixing unit 207 to a treatment substrate (e.g., an SCR device) 209 where nitrogen oxides are reduced to nitrogen and water.
0013<figref idref="f0002">FIG. 2</figref> shows an alternative system 220 that is substantially similar to the system 200 of <figref idref="f0001">FIG. 1</figref> except that a separate aftertreatment substrate 203 (e.g., a Diesel Particulate Filter (DPF) or Diesel Oxidation Catalyst (DOC)) is positioned between the engine 201 and the dosing and mixing unit 207. The pipe 202 carries the exhaust stream from the engine 201 to the aftertreatment substrate 203 and another pipe 204 carries the treated exhaust stream to the dosing and mixing device 207. <figref idref="f0003">FIG. 3</figref> shows an alternative system 240 that is substantially similar to the system 220 of <figref idref="f0002">FIG. 2</figref> except that the aftertreatment device 203 is combined with the dosing and mixing unit 207 as a single unit 205.
0014A selective catalytic reduction (SCR) catalyst device is typically used in an exhaust system to remove undesirable gases such as nitrogen oxides (NOx) from the vehicle's emissions. SCR's are capable of converting NOx to nitrogen and oxygen in an oxygen rich environment with the assistance of reactants such as urea or ammonia, which are injected into the exhaust stream upstream of the SCR through a doser. In alternative implementations, other aftertreatment devices such as lean NOx catalyst devices or lean NOx traps could be used in place of the SCR catalyst device, and other reactants (e.g., hydrocarbons) can be dispensed by the doser.
0015A lean NOx catalyst device is also capable of converting NOx to nitrogen and oxygen. In contrast to SCR's, lean NOx catalysts use hydrocarbons as reducing agents/reactants for conversion of NOx to nitrogen and oxygen. The hydrocarbon is injected into the exhaust stream upstream of the lean NOx catalyst. At the lean NOx catalyst, the NOx reacts with the injected hydrocarbons with the assistance of a catalyst to reduce the NOx to nitrogen and oxygen. While the exhaust treatment systems 200, 220, 240 are described as including an SCR, it will be understood that the scope of the present disclosure is not limited to an SCR as there are various catalyst devices (a lean NOx catalyst substrate, a SCR substrate, a SCRF substrate (i.e., a SCR coating on a particulate filter), and a NOx trap substrate) that can be used in accordance with the principles of the present disclosure.
0016The lean NOx traps use a material such as barium oxide to absorb NOx during lean burn operating conditions. During fuel rich operations, the NOx is desorbed and converted to nitrogen and oxygen by reaction with hydrocarbons in the presence of catalysts (precious metals) within the traps.
0017<figref idref="f0004 f0005 f0006">FIGS. 4-6</figref> show a dosing and mixing unit 100 suitable for use as dosing and mixing unit 207 in the treatment systems disclosed above. The dosing and mixing unit 100 includes a housing 102 having an interior 104 accessible through an inlet 101 and an outlet 109. A mixing tube arrangement 110 is disposed within the interior 104 (see <figref idref="f0005">FIGS. 5</figref> and <figref idref="f0006">6</figref>). With reference to the treatment systems 200, 220, 240, the inlet 101 receives exhaust flow from the engine 201 (or the treatment substrate 203) and the outlet 109 leads to the SCR 209. In certain implementations, the treatment substrate 203 also can be disposed within the housing 102 to form the combined unit 205 of <figref idref="f0003">FIG. 3</figref>.
0018As shown in <figref idref="f0005">FIG. 5</figref>, the housing 102 extends from a first end 105 to a second end 106 along a housing axis C. In an example, the housing axis C (i.e., an inlet axis) defines a flow axis for the inlet 101. The housing 102 also extends from a third end 107 to a fourth end 108 along a longitudinal axis L (i.e., outlet axis) of the mixing tube arrangement 110. In certain implementations, the housing axis C is not centered between the third and fourth ends 107, 108. In an example, the housing axis C is located closer to the third end 107. In certain implementations, the longitudinal axis L is not centered between the first and second ends 105, 106. In an example, the longitudinal axis L is located closer to the second end 106.
0019In an example, the longitudinal axis L defines a flow axis for the outlet 109. In certain implementations, the second end 106 is closed. In certain implementations, the second end 106 is curved to define a contoured interior surface 122. In an example, the second end 106 defines half of a cylindrical shape. In certain implementations, the third end 107 defines a port 140 at which a doser can be coupled (see <figref idref="f0004">FIG. 4</figref>). In other implementations, a doser can be disposed within the housing 102 at the third end 107.
0020As shown in <figref idref="f0006">FIG. 6</figref>, the housing 102 also has a first side 123 and a second side 124 that extend between the first and second ends 105, 106 and between the third and fourth ends 107, 108. In certain implementations, the first and second sides 123, 124 are closed. The closed second end 106 contours between the first and second sides 123, 124 (see <figref idref="f0006">FIG. 6</figref>). As shown in <figref idref="f0006">FIG. 6</figref>, the interior 104 of the housing 102 defines an inlet region 120 having a first volume and a mixing region 121 having a second, larger volume. The mixing region 121 extends from the inlet region 120 to the second end 106 of the housing 102. The mixing tube arrangement 110 is disposed within the mixing region 121.
0021As shown in <figref idref="f0006">FIG. 6</figref>, exhaust gas G flows from the inlet 101 towards the second end 106 of the housing 102. As the exhaust gas G approaches the mixing tube arrangement 110, some of the exhaust gas G begins to swirl within the housing interior 104. The mixing tube arrangement 110 causes the exhaust gas G to swirl about the longitudinal axis L (<figref idref="f0005">FIG. 5</figref>) of the mixing tube arrangement 110. In certain implementations, the mixing tube arrangement 110 defines slots 113 (which will be discussed in more detail below) through which the exhaust gas G enters the mixing tube arrangement 110. In certain implementations, the mixing tube arrangement 110 includes louvers 114 (which will be discussed in more detail below) that direct the exhaust gas G through the slots 113 in a swirling flow along a first circumferential direction D1 (<figref idref="f0006">FIG. 6</figref>).
0022A doser (or doser port) is disposed at one end of the mixing tube arrangement 110 (see <figref idref="f0005">FIG. 5</figref>). The doser is configured to inject reactant (e.g., aqueous urea) into the swirling flow G. Examples of the reactant include, but are not limited to, ammonia, urea, or a hydrocarbon. The doser can be aligned with the longitudinal axis L of the mixing tube arrangement 110 so as to generate a spray pattern concentric about the axis L. In other embodiments, the reactant doser may be positioned upstream from the mixing tube arrangement 110 or downstream from the mixing tube arrangement 110. The opposite end of the mixing tube arrangement 110 defines the outlet 109 of the unit 100. Accordingly, the reactant and exhaust gas mixture is directed in a swirling flow out through the outlet 109 of the housing 102.
0023In other implementations, the dosing and mixing unit 100 can be used to mix hydrocarbons with the exhaust to reactivate a diesel particulate filter (DPF). In such implementations, the reactant doser injects hydrocarbons into the gas flow within the mixing tube arrangement 110. The mixed gas leaves the mixing tube arrangement 110 and is directed to a downstream diesel oxidation catalyst (DOC) at which the hydrocarbons ignite to heat the exhaust gas. The heated gas is then directed to the DPF to burn particulate clogging the filter.
0024In some implementations, the mixing tube arrangement 110 is offset within the mixing region 121. For example, the mixing tube arrangement 110 can be disposed so that a cross-sectional area of the annulus is decreasing as the flow travels along a perimeter of the mixing tube arrangement 110. In the example shown, the mixing tube arrangement is located closer to the second side 124 than to the first side 123. In other implementations, however, the mixing tube arrangement 110 can be located closer to the first side 123. In some implementations, offsetting the mixing tube arrangement 110 guides the exhaust flow in the first circumferential direction D1. In some implementations, offsetting the mixing tube arrangement 110 inhibits exhaust gases G from flowing in an opposite circumferential direction.
0025For example, offsetting the mixing tube arrangement may create a high pressure zone 125 and a flow zone 126. The high pressure zone 125 is defined where the mixing tube arrangement 110 approaches the closest side (e.g., the second side 124). As the exterior surface of the mixing tube arrangement 110 approaches the housing side 124, less flow can pass between the mixing tube arrangement 110 and the side 124. Accordingly, the flow pressure builds and directs the exhaust gases away from the high pressure zone 125. The flow zone 126 is defined along the portions of the mixing tube 110 that are spaced farther from the wall (e.g., side wall 123, interior surface 122), thereby enabling flow between the mixing tube arrangement 110 and the wall.
0026In certain implementations, a portion of the mixing tube arrangement 110 contacts the closest side wall (e.g., side wall 124). For example, a distal end of a louver 114 (see <figref idref="f0007 f0008 f0009">FIGS. 7-9</figref>) of the mixing tube arrangement 110 may contact (see 128 of <figref idref="f0006">FIG. 6</figref>) the closest side wall 124. In such implementations, the contact 128 between the mixing tube arrangement 110 and the wall 124 further inhibits (or blocks) flow in the opposite circumferential direction.
0027<figref idref="f0007 f0008 f0009">FIGS. 7-9</figref> illustrate one example mixing tube arrangement 110 including a tube body 111 defining a hollow interior 112. The tube body 111 has a length L1. The tube body 111 has a slotted region 115 extending over a portion of the tube body 111. One or more slots 113 are defined through a circumferential surface of the tube body 111 at the slotted region 115. The slots 113 lead from an exterior of the tube body 111 into the interior 112 of the tube body 111. In some implementations, the slots 113 include axially-extending slots 113. In certain implementations, the tube body 111 defines no more than one axial slot 113 per radial position along the circumference of the tube body 111. In certain implementations, the slotted region 115 includes portions of the tube body 111 extending circumferentially between the slots 113 in the slotted region 115.
0028In some implementations, the slotted region 115 defines multiple slots 113. In certain implementations, the slotted region 115 defines between five slots 113 and twenty-five slots 113. In certain implementations, the slotted region 115 defines between ten slots 113 and twenty slots 113. In an example, the slotted region 115 defines about fifteen slots 113. In an example, the slotted region 115 defines about fourteen slots 113. In an example, the slotted region 115 defines about sixteen slots 113. In an example, the slotted region 115 defines about twelve slots 113. In other implementations, the slotted region 115 can define any desired number of slots 113.
0029As shown in <figref idref="f0008">FIG. 8</figref>, the slotted region 115 of the tube body 111 has a length L2 that is generally shorter than the length L1 of the tube body 111. In some implementations, the length L2 of the axial region 115 is shorter than the length L1 of the tube body 111. In certain implementations, the length L2 extends along a majority of the length L1. In certain implementations, the length L2 is at least half of the length L1. In certain implementations, the length L2 is at least 60% of the length L1. In certain implementations, the length L2 is at least 70% of the length L1. In certain implementations, the length L2 is at least 75% of the length L1. In some implementations, each slot 113 extends the entire length L2 of the axial region 115. In other implementations, each slot 113 extends along a portion of the axial region 115.
0030In some implementations, a ratio of the length L2 of the slotted region 115 to a tube diameter D (<figref idref="f0009">FIG. 9</figref>) is about 1 to about 3. In certain implementations, the ratio of the length L2 of the slotted region 115 to the tube diameter D is about 1.5 to about 2. In certain examples, the ratio of the length L2 of the slotted region 115 to the tube diameter D is about 1.75. In certain examples, the tube diameter D is about 12,7 cm (5 inches) and the length L2 of the slotted region 115 is about 20,32 cm (8 inches). In an example, each slot 113 of the slotted region 115 extends the length L2 of the slotted region 115.
0031As shown in <figref idref="f0009">FIG. 9</figref>, the slotted region 115 of the tube body 111 has a circumferential width S1 that is larger than a circumferential width S2 of a non-slotted region 116 of the tube body 111. The non-slotted region 116 defines a circumferential surface of the tube body 111 through which no slots are defined. In an example, the non-slotted region 116 defines a solid circumferential surface through which no openings are defined.
0032In some implementations, the circumferential width S2 of the non-slotted region 116 is significantly larger than a circumferential width of any portion of the tube body 111 extending between two adjacent slots 113 at the slotted region 115. For example, in certain examples, the circumferential width S2 of the non-slotted region 116 is at least double the circumferential width of any portion of the tube body 111 extending between two adjacent slots 113 at the slotted region 115. In certain examples, the circumferential width S2 of the non-slotted region 116 is at least triple the circumferential width of any portion of the tube body 111 extending between two adjacent slots 113 at the slotted region 115. In certain examples, the circumferential width S2 of the non-slotted region 116 is at least four times the circumferential width of any portion of the tube body 111 extending between two adjacent slots 113 at the slotted region 115. In certain examples, the circumferential width S2 of the non-slotted region 116 is at least five times the circumferential width of any portion of the tube body 111 extending between two adjacent slots 113 at the slotted region 115.
0033In some implementations, the circumferential width S1 of the slotted region 115 is substantially larger than the circumferential width S2 of the non-slotted region 116. In certain implementations, the circumferential width S1 of the slotted region 115 is at least twice the circumferential width S2 of the non-slotted region 116. In certain implementations, the circumferential width S1 of the slotted region 115 is about triple the circumferential width S2 of the non-slotted region 116.
0034In some examples, the slotted region 115 extends about 200° to about 350° around the tube body 111 and the non-slotted region 116 extends about 10° to about 160° around the tube body 111. In certain examples, the slotted region 115 extends about 210° to about 330° around the tube body 111 and the non-slotted region 116 extends about 30° to about 150° around the tube body 111. In an example, the slotted region 115 extends about 270° around the tube body 111 and the non-slotted region 116 extends about 90° around the tube body 111. In an example, the slotted region 115 extends about 300° around the tube body 111 and the non-slotted region 116 extends about 60° around the tube body 111. In an example, the slotted region 115 extends about 240° around the tube body 111 and the non-slotted region 116 extends about 120° around the tube body 111.
0035In some implementations, each slot 113 has a common width S3 (defined along the circumference of the tube body 111. In some implementations, the width S3 of each slot 113 is less than the circumferential width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is substantially less than the width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is less than half the width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is less than a third of the width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is less than a quarter of the width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is less than 20% the width S2 of the non-slotted region 116. In certain implementations, the width S3 of each slot 113 is less than 10% the width S2 of the non-slotted region 116.
0036In some implementations, the tube body 111 has a ratio of slot width S3 to tube diameter D (<figref idref="f0009">FIG. 9</figref>) of about 0.02 to about 0.2. In certain implementations, the ratio of slot width S3 to tube diameter D is about 0.05 to about 0.15. In certain implementations, the ratio of slot width S3 to tube diameter D is about 0.08 to about 0.12. In an example, the ratio of slot width S3 to tube diameter D is about 0.1. In certain examples, the slot width S3 is about 1,143 cm (0,45 inches) and the tube diameter D is about 12,7 cm (5 inches). In other implementations, however, the slots 113 can have different widths.
0037In some implementations, the slots 113 are spaced evenly around the circumferential width S1 of the slotted region 115. In such implementations, gaps between adjacent slots 113 within the slotted region 115 have a circumferential width S4. In certain implementations, the circumferential width S4 of the gaps is larger than the circumferential width S3 of the slots 113. In certain implementations, the circumferential width S3 of the slots 113 is at least half of the circumferential width S4 of the gaps. In certain implementations, the circumferential width S3 of the slots 113 is at least 60% of the circumferential width S4 of the gaps. In certain implementations, the circumferential width S3 of the slots 113 is at least 75% of the circumferential width S4 of the gaps. In certain implementations, the circumferential width S3 of the slots 113 is at least 85% of the circumferential width S4 of the gaps. In other implementations, however, the gaps between the slots 113 can have different widths.
0038In some implementations, the width S4 of each gap is less than the circumferential width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is substantially less than the width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is less than half the width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is less than a third of the width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is less than a quarter of the width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is less than 20% the width S2 of the non-slotted region 116. In certain implementations, the width S4 of each gap is less than 10% the width S2 of the non-slotted region 116.
0039In certain implementations, the slots 113 occupy about 25% to about 60% of the area of the slotted region 115. In certain implementations, the slots 113 occupy about 35% to about 55% of the area of the slotted region 115. In certain implementations, the slots 113 occupy less than about 50% of the area of the slotted region 115. In certain implementations, the slots 113 occupy about 45% of the area of the slotted region 115. In other words, the percentage of open area to closed area at the slotted region 115 is about 45%.
0040In some implementations, louvers 114 are disposed at the slotted region 115. In some implementations, each slot 113 has a corresponding louver 114. In other implementations, however, only a portion of the slots 113 have a corresponding louver 114. In some implementations, each louver 114 extends the length of the corresponding slot 113. In other implementations, a louver 114 can be longer or shorter than the corresponding slot 113.
0041As shown in <figref idref="f0009">FIG. 9</figref>, each louver 114 extends from a base 118 to a distal end 119 spaced from the tube body 111. In some implementations, the base 118 is coupled to the tube body 111. In other implementations, however, the base 118 can be spaced from the tube body 111 (e.g., suspended adjacent the tube body 111). In some implementations, the base 118 of each louver 114 is disposed at one end of a slot 113 so that the louver 114 extends at least partially over the slot 113 (e.g., see <figref idref="f0009">FIG. 9</figref>). In certain implementations, the louver 114 is sized to extend fully across the width S3 of the slot 113. In other implementations, the louver 114 extends only partially across the width S3 of the slot 1 13. In some implementations, the distal ends 119 of adjacent louvers 114 define gaps having a circumferential width S5. In certain implementations, the circumferential width S5 of the gaps is about equal to the circumferential width S3 of the slots 113 and the circumferential width S4 of the gaps.
0042In some implementations, each louver 114 extends straight from the slot 113 to define a plane. In certain implementations, the louvers 114 extend from the slot 113 at an angle θ relative to the tube body 111. In certain implementations, the angle θ is about 20° to about 70°. In an example, the angle θ is about 45°. In an example, the angle θ is about 40°. In an example, the angle θ is about 50°. In an example, the angle θ is about 35°. In certain implementations, the angle θ is about 30° to about 55°. In other implementations, each louver 114 defines a concave curve as the louver 114 extends away from the slot 113.
0043In some implementations, the tube body 111 has a louvered region over which the louvers 114 extend and a non-louvered region over which no louver extends. In some such implementations, the louvered region extends about 200° to about 350° around the tube body 111 and the non-louvered region extends about 10° to about 160° around the tube body 111. In certain examples, the louvered region extends about 210° to about 330° around the tube body 111 and the non-louvered region extends about 30° to about 150° around the tube body 111. In an example, the louvered region extends about 270° around the tube body 111 and the non-louvered region extends about 90° around the tube body 111. In certain examples, the louvered region largely corresponds with the slotted region 115. In an example, the louvered region overlaps the slotted region 115.
0044Various modifications and alterations of this disclosure will become apparent to those skilled in the art without departing from the scope of protection as defined in the appended claims, and it should be understood that the scope of this disclosure is not to be unduly limited to the illustrative embodiments set forth herein.
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| US2019351379A1 | United States of America | A1 | |
| US10960366B2 | United States of America | B2 | |
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| Dpma publication of mentioned ep patent grantGrantedR096 | R096 | DE | |
| European patents granted designating irelandGrantedFG4D | FG4D | IE | |
| European patent takes effect as a national patent in ch/liEP | EP | CH | |
| Reference to at number (ep patent validated in austria)REF | REF | AT | |
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Numbers
- Publication
- 3043894
- Application
- 147772248
Titles3
- German
- DOSIER- UND MISCHANORDNUNG ZUR VERWENDUNG BEI DER ABGASNACHBEHANDLUNG
- English
- DOSING AND MIXING ARRANGEMENT FOR USE IN EXHAUST AFTERTREATMENT
- French
- AGENCEMENT DE DOSAGE ET MÉLANGE POUR UTILISATION DANS UN POST-TRAITEMENT D'ÉCHAPPEMENT
Classification
- CPC, 18
- B01F23/2132
- B01F25/30
- F01N3/106
- F01N3/2066
- F01N3/2892
- F01N1/088
- F01N3/035
- F01N2240/20
- F01N2470/18
- F01N2610/02
- F01N13/009
- B01F2025/931
- B01F25/10
- B01F25/3131
- B01F23/20
- B01F25/00
- B01F2025/9121
- F01N3/20
- IPC, 3
- B01F5 00
- B01F5 04
- B01F3 04
Designated states38
- Contracting states, 38
- Albania
- Austria
- Belgium
- Bulgaria
- Switzerland
- Cyprus
- Czechia
- Germany
- Denmark
- Estonia
- Spain
- Finland
- France
- United Kingdom
- Greece
- Croatia
- Hungary
- Ireland
- Iceland
- Italy
- Liechtenstein
- Lithuania
- Luxembourg
- Latvia
and 14 moreShow fewer
- Monaco
- North Macedonia
- Malta
- Netherlands (Kingdom of the)
- Norway
- Poland
- Portugal
- Romania
- Serbia
- Sweden
- Slovenia
- Slovakia
- San Marino
- Türkiye
