• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Invention Patent: "STATIC MIXER FOR TREATING EXHAUST GASES AND METHOD OF MANUFACTURING THE SAME". The present invention relates to a static mixer (11) for the treatment of exhaust gases, comprising an annular support part (13) and a plurality of substantially coplanar radial fins (15) which are arranged radially with their parts or bases rear (17) associated with said support part (13) and the front parts or radial tips (19a) converging in the direction of the center ("G") of the mixer, where the body of the fins (15) comprises at least three lines bending, which define respective parts (15a, 15b, 15c) arranged in non-parallel planes and defining corresponding impact surfaces (A, B, C) for the exhaust gases.
    公开号:BR112013032764B1
    申请号:R112013032764-2
    申请日:2012-06-20
    公开日:2021-02-23
    发明作者:Pier Mario Cornaglia；Giorgio Villata
    申请人:Officine Metallurgiche G. Cornaglia S.P.A.；
    IPC主号:
    专利说明:

    Description Technical Field
    [001] The present invention relates to a static mixer for the treatment of exhaust gases and the method of manufacture thereof.
    [002] More precisely, the invention relates to a static mixer for the treatment of exhaust gases from internal combustion engines, which mixer can be incorporated into a system for the selective catalytic reduction (SCR) of nitrogen oxides. Prior Art
    [003] Static mixers are commonly used in order to promote the mixture of exhaust gases with the reducing agent, introduced in the gaseous or liquid state in the exhaust systems of internal combustion engines.
    [004] In this context, the static mixer is basically focused on promoting the formation of a highly homogeneous mixture and causing the maximum possible evaporation of the reducing agent introduced into the exhaust system.
    [005] In order to meet this requirement, static mixers are currently produced comprising a set of fins with various orientations within the duct where the mixture of exhaust gases and reducing agent flows.
    [006] The fins are generally associated with an annular structure designed to adhere to the internal walls of the duct that houses the mixer, which is generally arranged in a transversal way in the duct so that the flow of exhaust gas is intercepted by said fins.
    [007] The static mixer promotes the mixing of gases with the reducing agent, usually thanks to the increase in the phenomenon of turbulence within the exhaust gas flow.
    [008] Still, the supply of a static mixer in the region where the gas flow causes pressure increase within the exhaust system. Such a pressure increase is a disadvantage, since a problem with the exhaust gas discharge and, generally, can be more or less significant depending on the arrangement of the mixer and the exhaust system.
    [009] Furthermore, the surface of a mixer can cause condensation of the reduction mixture, with the consequent formation of a liquid film that adheres to the fins, thus causing a reduction in the efficiency of the same mixer.
    [0010] Thus, two phenomena must be contrasted when designing a mixer of the type mentioned above.
    [0011] The first phenomenon is determined by excessive pressure increases in the exhaust system housing the mixer. The second phenomenon is determined by the reduction of the mixing capacity, resulting from the formation of the condensed material of the reducing agent on the surfaces of the mixer.
    [0012] In an attempt to achieve the best compromise between opposing requirements for obtaining a good mix and preventing the above disadvantages from occurring, different solutions have been proposed.
    [0013] Some solutions use an array of fins from which the density, slope and size are chosen taking into account the requirements above. US 2007/0204751 describes an example of such a mixer.
    [0014] Other solutions use a set of fins, which are usually arranged radially inside the duct where the gases flow and are oriented so as to cause the mixture of said gases with the mixture of reducing agent. Static mixers of this second type are described, for example, in U.S. 7,533,520, US 2009/0320453 and U.S. 2009/0266064.
    [0015] In the solutions mentioned above, the effort to find the best compromise between mixing and free flow requirements for exhaust gases is clearly apparent.
    [0016] Notwithstanding these efforts, prior art mixers, however, do not completely solve the problem of how to obtain the best mix, while at the same time minimizing the above disadvantages.
    [0017] Furthermore, the efforts made so far result in solutions that are increasingly elaborate, complex and expensive to manufacture.
    [0018] In the field, therefore, there is still a strong need to have a static mixer available that is highly efficient, does not cause a significant pressure increase, and has little tendency to promote the formation of condensed material and does not have the above disadvantages related to manufacturing complexity and costs.
    [0019] Thus, it is a first objective of the invention to achieve such a result, by providing a static mixing device for the treatment of exhaust gases, which allows a better mixing in relation to the devices of the prior art and causes an increase in reduced pressure and reduced capacity to form condensed material.
    [0020] It is another object of the invention to provide a static mixer of the type discussed above, which can be manufactured industrially more simply and at lower costs than prior art mixers.
    [0021] It is additionally, but not the ultimate goal of the invention, to provide a mixer of the type discussed above, which can be employed substantially in any exhaust system in which selective catalytic reduction technology (SCR) is exploited.
    [0022] The above and other objectives are achieved by means of the static mixer for the treatment of exhaust gases and the manufacturing method of the same according to the attached claims. Description of the Invention
    [0023] A first advantage of the invention results from the provision of a plurality of radial fins, arranged within an annular perimeter, converging towards the center of the mixer and comprising at least three fold lines, which define an equal number of parts of fins arranged in non-parallel planes and defining corresponding impact surfaces for the exhaust gases.
    [0024] Thanks to said arrangement, the mixer is able to cause the formation of a turbulent flow with a swirl in the flow of gas and urea flowing through it and consequently to cause an effective mixture of urea with the exhaust gases.
    [0025] The plurality of fold lines and the corresponding impact surfaces formed, thus, in the mixer fins advantageously assist in increasing the general surface against which the urea jet impinges, thus determining a high nebulization. In addition, such distribution contributes to the reduction of the phenomenon of creating a liquid film downstream of the mixer, a film which, as is known, reduces the mixing performance.
    [0026] Another advantage of the invention results from the supply, in the mixer, of a free central part, that is, a part having no obstacles to the free flow of the exhaust gases, in the direction of which the radial fins converge. Thanks to such a free central part and the shape of the radial fins, it is possible to obtain an effective mixing effect of the exhaust gases with the mixture of reducing agent. Such mixing effect is promoted by the presence of said central hole, which, on the other hand, contributes to prevent an excessive increase in pressure due to the supply of the mixer. In fact, in correspondence with the central bore, an increase in gas velocity and an intense forward propulsion of the gases occur, resulting in an advantageous turbulent movement downstream of the mixer.
    [0027] An additional advantage of the invention results from the probability of manufacturing the mixer by means of a succession of simple cutting and edge operations. Brief Description of the Figures
    [0028] Some preferred embodiments of the invention will now be described with reference to the attached Figures, in which:
    [0029] Figure 1 is a front perspective view of the mixer according to the invention;
    [0030] Figure 2 is a plan view of the mixer shown in Figure 1;
    [0031] Figure 3 is a side view of the mixer shown in Figure 1;
    [0032] Figure 4 is a cross-sectional view taken along line IV-IV in Figure 2;
    [0033] Figure 5 is a schematic view of an exhaust system incorporating the mixer;
    [0034] Figure 6 is a plan view of the mixer, in a first stage of work;
    [0035] Figure 7 is a cross-sectional view taken along a longitudinal plane of the mixer, in a second work step;
    [0036] Figure 8 is a front perspective view of the mixer, in a third stage of work. Description of a Preferred Modality
    [0037] With reference to Figures 1 to 4, the static mixer for the treatment of exhaust gases according to the invention was generally denoted by the numerical reference 11.
    The mixer 11 includes an annular support part 13 and a plurality of substantially coplanar radial fins 15, which are radially arranged and have their rear ends or bases 17 associated with said support part 13 and their front ends or radial tips 19 converging towards the center "G" of the mixer.
    [0039] According to the invention, the body of each fin 15 comprises at least three fold lines 11, 12, 13, which define an equal number of parts 15a, 15b, 15c arranged in non-parallel planes and defining surfaces of corresponding impact factors A, B, C for the exhaust gases. Preferably, in addition, said impact surfaces A, B, C are substantially flat.
    [0040] Still according to the invention, the radial tips 19 of fins 15 surround a central part 21 of the mixer. Said part 21, which is substantially circular in the illustrated example, is free, that is, it is not occupied by the fins or other parts of the mixer and defines an interference-free passage for the exhaust gases.
    [0041] Always according to the invention, the impact surfaces A, B, C for the exhaust gases are in non-parallel planes with respect to a transverse plane "P" in which the mixer is located and which substantially corresponds to the plane of the sheet comprising Figure 2. Said planes on which the impact surfaces are located are, therefore, not perpendicular to the direction of flow of the exhaust gases passing through the mixer, the said direction being denoted by the arrow " F "in Figure 3. In addition, the planes on which the impact surfaces A, B, C meet are parallel to each other and intersect the gas flow and the reduction mixture according to different angles. Preferably, said angles decrease from the fin base 17 towards the periphery.
    [0042] In a preferred embodiment of the invention, a first impact surface A adjacent to the base 17 of the fin 15 is inclined by an angle in the range of 30 to 60 with respect to said transverse plane P of the mixer. In the illustrated embodiment, the first impact surface A is also substantially shaped like a rectangular trapezoid.
    [0043] Always according to a preferred embodiment of the invention, a second impact surface B adjacent to the first impact surface A is inclined by an angle in the range of 40 to 70 with respect to the first impact surface A. In the illustrated embodiment , the second impact surface B is also substantially rectangular.
    [0044] Still according to a preferred embodiment of the invention, a third impact surface C adjacent to the second impact surface B is inclined by an angle in the range of 20 to 50 with respect to the second impact surface. In the illustrated embodiment, the third impact surface C is substantially triangular and furthermore defines an axial tip 19b longitudinally directed towards the front region of the mixer 11, from where the exhaust gases arrive.
    [0045] Preferably, according to the invention, the impact surfaces A, B, C define in total a concave part for each wing, with the concavity turned in the posed direction with respect to the gas flow direction "F ".
    [0046] The annular support part 13 includes a crown 13a, preferably closed to form a ring, which in the illustrated example defines a circular inner perimeter 13b and a circular outer perimeter 13c for the mixer 11. Other modalities will, however, be , possible, in which the inner perimeter 13b and / or outer perimeter 13c have a different shape than the circular, for example, an octagonal, hexagonal, square or rectangular shape. In yet other embodiments, the fins 15 can be directly associated with the internal part of the duct of the exhaust system housing the mixer. In such a case, the annular support 13 will be an integral part of the duct.
    [0047] According to a preferred embodiment of the invention, the fins 15 are angularly spaced evenly along the inner perimeter 13b of the annular support part 13.
    [0048] Always with reference to a preferred modality of the invention, eight radial fins 15 are provided. The ideal number of fins 15 can, however, be chosen depending on the characteristics of the exhaust system into which the mixer is incorporated, and generally any number of fins can be provided. In this way, other modes of the mixer will be possible, where the number of fins is different from eight. A number of fins ranging from four to sixteen is considered responsible for the least performance.
    [0049] Furthermore, in a preferred embodiment, the diameter of the circular central part 21 is about 1/4 of the diameter of the internal perimeter 13b of the mixer.
    [0050] Altogether, within the internal perimeter 13b, the mixer 11 has a region occupied by the plurality of fins 15 intercepting the exhaust gases and the mixture of reducing agent, and a free region formed by the zones included between the fins and denoted by reference number 23, in addition to the central part 21.
    [0051] With reference to Figure 5, a unit 111 is schematically illustrated for the treatment of exhaust gases from an internal combustion engine, where SCR technology is used. Said unit 111 comprises a set of ducts for the exhaust gases, housed within a envelope 113. The static numerical reference 115, in which the exhaust gases flow in the direction indicated by the arrow "F". In the illustrated example, mixer 11 is transversely disposed within duct 115, the region immediately downstream 117 where the reducing agent mixture is introduced. Always with reference to the illustrated example, the mixture of reducing agent is introduced by injection by means 119 preferably including a nozzle or a suitable valve and axially arranged at the beginning of duct 115, in the direction of the exhaust gas flow. Said duct 115 further comprises, between the devices 119 and the mixer 11, a radially oriented exhaust gas inlet 121, formed by a corresponding part of the duct 115 provided with the radial holes 123.
    [0052] According to the configuration above, which corresponds to the preferred but not exclusive arrangement, the exhaust gases enter radially in duct 115 and are intercepted by the reducing agent reaching the axial direction, that is, 90 in relation to the direction of gas inlet. Thus, the exhaust gas flow reaches the axial direction, that is, it is deformed by about 90 with respect to the inlet direction in the duct 115, in the mixer 11, which occupies substantially the entire cross section of the duct 115.
    [0053] Advantageously, according to the invention, the mixer 11 can be manufactured by means of a succession of simple work operations.
    [0054] According to a preferred method of manufacture, the mixer is obtained from a laminated metal body having a thickness preferably ranging from 0.8 to 2.0 mm, and more preferably 1.5 mm. The fins 15 will therefore have substantially a laminar consistency.
    [0055] Preferably, as will be explained hereinafter, the mixer is manufactured by means of mechanical cutting and bending operations. Alternatively, the mixture can also be manufactured by other mechanical works, for example, grinding or electron discharge machining.
    [0056] In a preferred embodiment of the mixer manufacturing method, which will be described later, the machining of a flat laminar metal body, for example, a laminated metal sheet, is carried out.
    [0057] With reference to Figure 6, the initial product is illustrated, comprising a flat body 11 'obtained, for example, by cutting or shearing a flat sheet of laminated metal.
    [0058] In the illustrated example, the body 11 'is disk-shaped with an outer diameter of about 140 mm and comprises eight fins 15' spaced at an even angle. In this work stage of the mixer, and always with reference to the illustrated example, the fins 15 'have a substantially flat triangular shape and one of its vertices is directed towards the center "G" of the disk-shaped body. More precisely, always with reference to the illustrated example, the fins 15 'are shaped as isosceles triangles with the base angles of about 70 and the apex angle of about 45.
    [0059] The raw fins 15 'are subsequently folded along the fold lines 11, 12, 13, for example, by means of a robotic manipulator, thus obtaining the final product corresponding to the mixer 11 described with reference to the Figures of 1 to 4.
    [0060] In a preferred embodiment of the invention, in order to make the folding of the fins 15 'easier and to reduce the extension of the impact surfaces of the fins when the mixer is closed, and thus to limit the increase of pressure inside the duct that will house the mixer, the body 11 'undergoes the removal of material in a more or less wide band around the fins. Said band is denoted by the numerical reference 10 in Figure 6 and extends around the fins, with the exception of an appendix 17 'connecting the fins to the support part 13'.
    [0061] Figure 7 illustrates a subsequent step of manufacturing the mixer, in which the fins 15 '' were obtained by folding the fins 15 'illustrated in Figure 6 around the first fold line 11. A second fold along the second fold line 12 allows obtaining the body 11 '' 'illustrated in Figure 8, and a third fold along the third fold line 13 allows obtaining the mixer 11 in its final shape, illustrated in Figures 1 to 4.
    [0062] It should be appreciated that the support part 13 of the mixer can also undergo work, for example, a drawing, starting from the flat part 13 'in order to obtain the "L" shaped section illustrated in Figure 4.
    [0063] Altogether, the method according to the invention comprises the steps of: - providing a substantially flat laminar metallic body 11 '; - forming in said laminated metal body, for example, by cutting the laminated metal, a plurality of radial fins 15 'radially arranged and substantially coplanar; - fold fins 15 'around a first fold line 11, thereby obtaining fold fins 15' '; - the folding of folded fins 15 "around a second fold line 12, thus obtaining double folded fins 15" '; - the folding of double fold fins 15 "" around a third fold line 13, thus obtaining the mixer 11.
    [0064] Various changes and modifications, included within the same inventive principle, can be made in the static mixer as described and illustrated.
    权利要求:
    Claims (10)
    [0001]
    1. Static mixer (11) for the treatment of exhaust gases, comprising an annular support part (13) and a plurality of substantially coplanar radial fins (15) which are arranged radially with their associated back or base (17) with said support part (13) and the front or radial tip (19a) converging in the direction of the center ("G") of the mixer, characterized in that the body of the fins (15) comprises at least three fold lines , which define the respective parts (15a, 15b, 15c) arranged in non-parallel planes and defining corresponding impact surfaces (A, B, C) for the exhaust gases.
    [0002]
    2. Mixer, according to claim 1, characterized by the fact that said impact surfaces (A, B, C) for the exhaust gases are in non-parallel planes with respect to the intermediate transverse plane of the mixer (11) and are therefore not perpendicular to the flow direction ("F") of the exhaust gases passing through the mixer.
    [0003]
    3. Mixer according to claim 2, characterized by the fact that a first impact surface (A) adjacent to the base of the fin is inclined at an angle between 30o and 60o with respect to the intermediate transverse plane of the mixer.
    [0004]
    4. Mixer according to claim 3, characterized by the fact that a second impact surface (B) adjacent to the first impact surface (A) is inclined at an angle between 40o and 70o with respect to the first impact surface ( THE).
    [0005]
    5. Mixer according to claim 4, characterized by the fact that the third impact surface (C) adjacent to the second impact surface is inclined at an angle between 20o and 50o with respect to the second impact surface.
    [0006]
    6. Mixer, according to any one of the preceding claims, characterized by the fact that said impact surfaces define a concave part for each fin (15).
    [0007]
    7. Mixer according to any one of the preceding claims, characterized in that the radial tips (19a) of the fins (15) surround a free central part (21) of the mixer for the passage of gases.
    [0008]
    8. Mixer according to any one of the preceding claims, characterized in that the fins (15) are evenly spaced at an angle.
    [0009]
    9. Mixer according to any one of the preceding claims, characterized by the fact that the fins (15) are four to sixteen in number.
    [0010]
    10. Method of manufacturing a static mixer, as defined in any one of claims 1 to 9, characterized by the fact that the steps of: providing a substantially flat laminar body (11 ') made of metal are provided; providing said metal body, for example, by cutting the laminar body, with a plurality of radial fins (15 ') arranged radially and substantially mutually coplanar; subjecting the fins (15 ') to a folding operation along a first folding line (l1), thereby obtaining folded fins (15 "); subjecting the folded fins (15') to a folding operation along a second fold line (l2), thus obtaining double fold loops (15 "); subjecting the fins (15 ") to a bending operation along a third bending line (13), thus obtaining the mixer (11).
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    法律状态:
    2018-12-11| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|
    2020-01-14| B06U| Preliminary requirement: requests with searches performed by other patent offices: procedure suspended [chapter 6.21 patent gazette]|
    2020-12-15| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|
    2021-02-23| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 20/06/2012, OBSERVADAS AS CONDICOES LEGAIS. |
    优先权:
    申请号 | 申请日 | 专利标题
    IT000535A|ITTO20110535A1|2011-06-20|2011-06-20|STATIC MIXER FOR THE TREATMENT OF EXHAUST GAS AND ITS MANUFACTURING METHOD.|
    ITTO2011A000535|2011-06-20|
    PCT/IB2012/053102|WO2012176127A1|2011-06-20|2012-06-20|Static mixer for the treatment of exhaust gases and manufacturing method thereof|
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