• 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:
    In order to be able to easily adjust the dilution ratio of a Venturi diluent and to be able to easily clean the Venturi diluter, a housing (2) is provided in which a compressed air nozzle body (5) and an outlet nozzle body (7) are inserted axially spaced in a recess (6) A mixing chamber (8) is formed in the recess (6) between the compressed-air nozzle body (5) and the outlet nozzle body (7) and the compressed-air nozzle body (5) and / or the outlet nozzle body (7) are inserted interchangeably; 8) is provided, which opens into the mixing chamber (8) and which is connected to a compressed-air line (3) in the housing (2), and at the mixing chamber (FIG. 8) facing the axial end of the outlet nozzle body (7) an outlet nozzle recess (10) is provided, which opens into the mixing chamber (8) and in a flared Aus- passage chamber (11) merges and on the housing (2) an aerosol line (4) is provided which opens into the mixing chamber (8).
    公开号:AT514381A1
    申请号:T50232/2013
    申请日:2013-04-04
    公开日:2014-12-15
    发明作者:
    申请人:Avl List Gmbh；
    IPC主号:
    专利说明:

    AV3535 AT
    Venturiverdünner
    The subject application relates to a Venturi diluent and the use of the Venturi diluent® in a particle generator for generating an aerosol.
    To dilute particle-loaded gas (aerosol), e.g. with clean air, are used among other 5 so-called Venturi thinner, which operate on the ejector principle. In this case, particle-free air is passed through an annular gap arranged concentrically around an aerosol inlet nozzle (in the form of a valve nozzle) and generates thereon a negative pressure which is proportional to the square of the flow velocity in the annular gap. This negative pressure draws in through the aerosol inlet nozzle an aerosol volume flow which is absorbed by the 10 th nozzle cross section has the same speed as the clean air flow. One speaks therefore also of a Venturi pump. The ratio of the two Volurnenströrrie, and thus the degree of dilution depends on the free cross-sections of the annular gap and the aerosol inlet nozzle and can be adjusted. The flow cross-section widens after the nozzle arrangement to a mixing chamber in which the two air streams mix. From the mixing chamber then the required dilute aerosol can be removed. In such venturi diluents for diluting aerosols, the cross-section of the annular gap or the diameter of the inlet nozzle during operation contaminates quickly, especially in combustion gases with proportions of combustion soot, and difficult, if not impossible to clean. Due to the contamination and the associated change in the cross section, however, the degree of dilution changes greatly and uncontrollably, which means that the Venturi diluent is currently unusable. In addition, the dilution ratio can not be adjusted, but is determined by the annular gap and the diameter of the inlet nozzle. At best, several such venturi diluents may be cascaded to achieve higher dilution factors. It is therefore an object of the present invention to provide an easy-to-clean Venturi diluent with a simple, accurate and reliably adjustable dilution ratio.
    This object is achieved by a Venturi thinner with the features of claim 1. By virtue of the fact that at least the compressed-air nozzle body or the outlet nozzle body can be exchanged, on the one hand the dilution ratio can be adjusted very simply and accurately by using nozzle bodies with different flow cross-sectional areas and, on the other hand, the part of the Venturi thinner which suffers from particle deposits and contamination, very easily accessible from the outside for cleaning. Simple cleaning can cause an uncontrolled change in the dilution ratio-2 / 1Ö1
    AV-3535 AT nicles are prevented by Ryle deposits in the Venturi diluent, which makes the set dilution ratio also very reliable.
    The subject invention will be explained in more detail with reference to Figures 1 and 2, the exemplary, schematic and non-limiting advantageous embodiments of the invention 5 show. It shows
    Fig. 1 shows a venturi thinner according to the invention and
    2 shows the use of the venturi thinner in a particle generator.
    The venturi 1 according to the invention shown in Fig. Consists of a housing 2 in which a compressed air line 3, an aerosol line 4 is provided. In the housing 2, a compressed air nozzle body 5 is inserted in 1 o a corresponding recess 6, preferably screwed. Furthermore, in the housing 2 in the recess 6, an outlet nozzle body 7 is inserted, preferably screwed. The compressed air nozzle body 5 and the outlet nozzle body 7 are arranged axially spaced in the recess 6, so that a mixing chamber 8 is formed therebetween. On the mixing chamber 8 facing axial end of the compressed air nozzle body 5 a Druckluftdüsenausnehmung 9 is provided, which opens into the mixing chamber 8 and which is connected to the Druekluftleitung 3. The Druckluftdüsenausnehmung 9 is preferably designed as an axial bore and has a diameter A and a cross-sectional area ÄA. The compressed air nozzle body 5 is designed to be conically conical in the area of the mixing chamber 8, wherein the cone angle α is preferably in the region of 7 °.
    In the outlet nozzle body 7, an outlet nozzle recess 10 is provided on the axial end facing the mixing chamber 8, which is connected to the mixing chamber 8 and which is connected to an outlet chamber 11 arranged at the other axial end. The Austrittdüsenausnehmung 10 is preferably designed as an axial bore and has a diameter B B or a cross-sectional area AB. The mixing chamber 8 facing axial end of the outlet nozzle body 7 in the form of an inner cone, wherein the cone angle ß preferably in the range of 30 ° to 50 °, typically at 45 °. The outlet chamber 11 is widened with respect to the Austrittdüsenausnehmung 10, that is designed with a cross section greater than the cross section AB. The transition from the outlet nozzle to the outlet chamber 11 is preferably conical, the angle of reflection γ preferably being in the range of 50 ° to 70 °, typically 60 °.
    The aerosol line 4 preferably opens in the region of the outer cone of the compressed-air nozzle body 5 into the mixing chamber 8, so that the supplied aerosol deflects wildly on the cone. The specified cone angles α, β, γ ensure particularly favorable flow conditions in the 3 / 1Ö2 '
    AV3535 AT
    Venturi Diluent 1. At the exit chamber 11, a conduit can be connected to remove dilute aerosol from the venturi diluent 1.
    The Druckluftdüsenausnehmung 9 and the Austrittdüsenausnehmung 10 are preferably arranged in alignment. The cross section AB of the Austrittdüsenausnehmung 10 is smaller than the cross section Aa of Druckluftdüsenausnehmung 9. About the compressed air line 3 compressed air is supplied with overpressure. The compressed air flows through the Druckluftdüsenausnehmung 9 in the mixing chamber 8 and from there into the Austrittdüsenausnehmung 10. Due to the change in cross section is formed in the region of the Austrittdüsenausnehmung 10 a negative pressure, the aerosol sucks into the mixing chamber 8. The sucked in 1 o Aerosol is entrained by the compressed air flow and mixed with the compressed air or diluted by the compressed air. The suppression and thus the dilution ratio is determined by the ratio of the diameter A to B, or generally by the ratio of the cross-sectional areas Aa to AB. If the diameter B is assumed to be 3 mm, at diameters A of 1 mm, 1.5 mm and 2 mm, e.g. Dilution ratios of 1: 8, 1: 5 and 1: 3. Thus, the dilution ratio is easily adjustable by replacing the compressed air nozzle body 5 and / or the discharge nozzle body 7 or by changing the diameter A and / or B or the cross-sectional areas Aa and / or AB. For example, For example, sleeves with different inner diameters could be inserted into the compressed air nozzle body 5 and / or the exit nozzle body 7 to change the diameter A 20 and / or B or the cross-sectional areas Aa and / or AB.
    Due to the interchangeability of compressed air nozzle body 5 and outlet nozzle body 7, the venturi thinner 1 but also easy to clean.
    FIG. 2 schematically illustrates the exemplary application of the Venturi diluter 1 according to the invention in a particle generator 20. In this case, an Ae-25 rosol is produced in a burner 21. Such burners 21 are well known and commercially available, so will not be discussed further here. Downstream of the burner 21, a so-called Volatile Particle Remover (VPR) 22 is connected to which the aerosol generated in the burner 21 is supplied via an aerosol line 24.
    Between burner 21 and VPR 22, a first outlet conduit 25 may be connected, so out through the undiluted aerosol from the burner 21 to the outside and for further external use, e.g. for calibration of a particle analyzer.
    Volatile Particle Removers (VPR) 22 are also well known devices for diluting aerosols. The VPR 22 shown here comprises an input-side 4 / 1Ö3 '
    AV-3535 AT hot dilution stage 26, an evaporation tube 27 and an outlet cold dilution stage 28. In the hot dilution stage 26, e.g. carried out as a dilution tunnel or as a rotary diluent as described in EP 2 025 979 A1, the aerosol coming from the burner 21 is diluted with filtered, preferably heated, air, which is fed via line 29 to a line 29. Evaporation Tube 27 removes volatile components in the aerosol. For this purpose, the first dilution stage 26 and the evaporation tube 27 can also be arranged in a heated chamber 30. Evaporation tube 27 is followed downstream by a cold dilution step 28, e.g. is designed in the form of a venturi thinner 1 according to the invention. Instead of the inventive Venturi diluent 1, any other Venturi diluent or any other suitable diluent could be used. An example of a VPR 22 is also described in EP 2 264 423 A2. An output dilution stage 23 is disposed downstream of the VPR 22 and connected by the aerosol conduit 24.
    Between VPR 22 and output dilution stage 23, a second exit conduit 31 15 may be connected, passed outwardly through the dilute aerosol from the VPR 22, and for further external use, e.g. for calibration of a particle analyzer.
    The output dilution stage 23 is embodied here as a dilution bridge 34, in which the aerosol stream is split into two parallel substreams, a first substream being passed over a HEPA filter (High Efficiency Particulate Air Filter) 32 in which a further dilution of the aerosol takes place. In the other second partial flow, a controllable valve 33 is arranged, with which the volume flow over the first partial flow, and thus the degree of dilution, can be adjusted. The two partial flows are brought together again after the HEPA filter 32 and the valve 33. Following dilution bridge 34, another dilution step, e.g. in the form of another venturi diluent 1 according to the invention. Instead of the Venturi diluent 1 according to the invention, any other Venturi diluent or any other suitable diluent could also be used.
    The output from the output dilution stage 23 is led out to the outside as the third output conduit 36 of the particle generator 20 and for further external use, e.g. for a calibration of a particle measuring device, made accessible.
    The particle generator 20 described above thus has three outputs at which aerosol with different particle concentrations and different particle sizes can be taken. For example, Aerosol with particles in the size of 10-120nm and a 35 concentration of up to 5 x 107 particles / cm3 on the first output line 25 after the 5 / 1Ö4 '5
    AV3535 AT
    Burner 21, aerosol with particles in the large of 5-100nm and a concentration of up to 1 x 107 particles / cm3 on the second output line 31 after the VPR 22 and aerosol with particles in the size of 5-100nm and a concentration of up to to 1 x 101 particles / cm 3 on the third output line 36 after the output dilution stage 23, 1/105 '
    权利要求:
    Claims (2)
    [1]
    AV-3535 AT Claims 1. Venturi diluent with a housing (2) into which a compressed air nozzle body (5) and an outlet nozzle body (7) are inserted axially spaced in a recess (6), so that in the recess (6) between compressed air nozzle body (5) and outlet nozzle body (7) forms a mixing chamber (8) and the compressed air nozzle body (5) and / or the outlet nozzle body (7) are used interchangeably, wherein at the mixing chamber (8) facing the axial end of the compressed air nozzle body (5) Compressed-air nozzle recess (9) is provided which opens into the mixing chamber (8) and which is connected to a compressed air line (3) in the housing (2), and wherein an axial end of the outlet nozzle body (7) facing the mixing chamber (8) Provision nozzle recess (10) is provided, which opens into the mixing chamber (8) and which merges into a flared outlet chamber (11) and on the housing (2) an aerosol line (4) is provided, which in di e mixing comb he (8) opens.
    [2]
    2. Use of the Venturi thinner according to claim 1 in a particle generator (20) 15 for generating an aerosol. -6- 7/10
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    同族专利:
    公开号 | 公开日
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    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    CH585064A5|1974-10-08|1977-02-28|Lenzburg Sauerstoffwerk Ag|Mixing nozzle for balloon gases - e.g. air and helium, having variable mixture ratio control valve|
    DE3436624A1|1984-10-05|1986-04-10|Norddeutsche Affinerie AG, 2000 Hamburg|DEVICE FOR GENERATING FLAMMABLE SOLID / GAS SUSPENSIONS|
    US6042089A|1996-07-01|2000-03-28|Klein; Christophe|Foam generating device|
    WO2002071030A1|2001-03-02|2002-09-12|Parsons Advanced Technologies Inc.|Particulate and gaseous emission testing method and apparatus|
    US7784999B1|2009-07-01|2010-08-31|Vortex Systems Ci|Eductor apparatus with lobes for optimizing flow patterns|
    US778499A|1904-11-18|1904-12-27|Laval Steam Turbine Co|Elastic-fluid turbine.|
    AT9603U3|2007-08-16|2008-08-15|Avl List Gmbh|ROTATION THINNER FOR FLUID FLOWS|
    AT10541U3|2009-01-13|2009-11-15|Avl List Gmbh|DEVICE FOR DETERMINING THE CONCENTRATION OF SOLID PARTICLES|DE202015105290U1|2015-10-06|2017-01-11|Nordson Corporation|Cleaning station for needle nozzles|
    DE102017130981B3|2017-12-21|2019-06-19|Horiba Europe Gmbh|System for providing an aerosol|
    IT201900000979A1|2019-01-23|2020-07-23|Particular Mat S R L|PERFECTED MIXER FOR THE PRODUCTION OF NANOMATERIALS|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50232/2013A|AT514381B1|2013-04-04|2013-04-04|Venturiverdünner|ATA50232/2013A| AT514381B1|2013-04-04|2013-04-04|Venturiverdünner|
    DE201410104849| DE102014104849A1|2013-04-04|2014-04-04|Venturiverdünner|
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