• 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:
    The presterilization of packaging machines for the manufacture of aseptic packing containers can be carried out with the help of sterile air and liquid sterilizing agent, which are blended so that a gas saturated with sterilizing agent of a suitable temperature and dew point is obtained. In order to achieve a rapid and effective volatilization of the liquid a circulating movement is imparted to the hot sterile air at the same time as the sterile liquid is introduced into the centre of the circulating movement. An arrangement for the realization of this comprises a chamber (1) with a helical guide rail (6) and a spray nozzle (7) for the sterilizing liquid.
    公开号:SU1386018A3
    申请号:SU843695566
    申请日:1984-01-24
    公开日:1988-03-30
    发明作者:Хильмерссон Андерс；Лагерстедт Ян；Андерссон Хельге
    申请人:Тетра Пак Интернэшнл Аб (Фирма)；
    IPC主号:
    专利说明:


    SP
    The invention relates to a technique for the evaporation of a liquid, by mixing it with a heated gas.
    The aim of the invention is to increase the efficiency and thereby obtain a mixture with a higher dew point and a much larger volume per unit of time suitable for pre-sterilization of packaging machines.
    An example of the method. The sterilizing fluid consisting of hydrogen peroxide serves B a vertical cylindrical chamber from above along the central axis in the form of droplets and at the same time serves air heated to 300 ° C at a speed of 150 m / s along with it circulating movement along the trajectory of the cylindrical spiral where the central axis of the spiral is cameras.
    Air can also be supplied in countercurrent of sterilizing liquid in the form of droplets of 10-80 microns in size. The droplet size is so chosen because the spray nozzle produces droplets mainly within these limits,
    The drawing shows a device for the evaporation of a sterilizing liquid with a partial cut.
    The device comprises a vertical cylindrical mixing chamber 1 surrounded by a housing with a cylindrical side wall 2 and end walls 3. In addition, there are inlet and outlet pipes 4 and 5, respectively, which are connected to the cylindrical wall 2 tangentially. The inlet pipe 4 is located near the lower end wall of the mixing chamber, and the outlet pipe 5 is adjacent to the upper end wall 3 of the mixing chamber 1. The cylindrical wall 2, the end walls 3 and the pipelines 4 and 5 are made of stainless steel, the wall 2 having a relatively large thickness of about 5 mm. The total height of the chamber is 0.5 m, and the diameter is 150 mm.
    A spiral guide 6 is installed inside the chamber 1, passing along the surface of the side wall between the two end walls. The guide 6 is made of a strip of material in the form of a spiral, while its width decreases from 60 mm at the upper end of the mixing chamber
    ,
    , ten
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    thirty
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    82
    UP TO 20 mm at the lower end of the mixing chamber. Since the guide 6 with its one edge is located on the inner surface of the side wall 2, a gradual reduction in its width means that the guide has a central conical opening with a cone angle of 15®.
    In the mixing chamber 1 there is a nozzle 7 installed in the center of the upper end wall 3. The outlet of the nozzle 7 is located in the chamber immediately behind the inner surface of the end wall 3, and its central position means that the outlet of the nozzle is on the continuation of the geometric central axis, common for the guide 6 in the form of a spiral and the cylindrical wall 2 of the mixing chamber .1. The nozzle 7 is made of a spray type, forms droplets of 10 to 80 µm in size, which are sprayed in the form of a conical jet, the ANGLE of the cone of which is about 15 and, thus, corresponds to the conical angle of the center hole of the guide. 6. Outside the chamber, the nozzle 7 is connected through a valve to the supply lines 9 and 10 for liquid and gas, respectively. Pipeline
    9 is connected to a liquid tank (not shown) and the pipe 10 to a source of sterile air.
    When the device is installed in a packaging machine, the feed and discharge pipes are connected to the machine system of sterile air and sterilizing fluid, respectively.
    The device works as follows.
    Before starting pre-sterilization, hot sterile air is supplied through the inlet pipe 4 at a speed of 150 m / s. Since the inlet pipe 4 is tangential to the wall 2, a circulating motion is connected to the air. By means of the guide 6, the circulating air rises upward in the mixing chamber 1 and gradually reaches the exhaust pipe 5, also connected tangentially. After the passage of hot air through the mixing chamber 1, when the latter is heated for a certain time to the air temperature, i.e. 300 ° C, hydrogen peroxide and sterile air are supplied under high pressure through pipelines 9 and 10, respectively, to nozzle 7. The sterilizing fluid is injected through the nozzle outlet to the mixing chamber 1 in countercurrent with respect to the air flow, i.e. way down. The nozzle 7 injects liquid in the form of droplets with a size of 10-80 µm and sprays it in the form of a uniform conical jet with a cone angle of 15 °. Since the circulating movement is connected to gas or hot air moving along the walls of the mixing chamber 1, the sterilizing liquid entering through the nozzle 7 is supplied to the center of the circulating movement and, in particular, along the central axis of the spiral movement of gas. The smaller sterilizing liquid droplets exiting the nozzle 7 mix very quickly with the rotating hot air and evaporate, while the medium and large size drops further down into chamber 1 until they are heated to such an extent as to evaporate. Epagodar counterflow principle larger drops upon reaching the lower end of the mixing chamber 1 meet with hot air with a higher temperature, which guarantees good evaporation even of relatively large drops of sterilizing agent. The spiral movement of hot air means that the drops, when they are trapped by hot air, are entrained by them (although they evaporate) to the periphery of the mixing chamber, where (if they have not reached earlier evaporation) they contact the cylindrical wall 2 of the mixing chamber 1, which heated by hot air to a high temperature, and immediately evaporated.
    The injection of the sterilizing liquid into the mixing chamber is preferably carried out periodically at such intervals as to produce air saturated with the sterilizing agent, with an appropriate dew point. Between the injections, the cylindrical wall 2, due to its greater thickness, can absorb and store the thermal energy of the passing hot air. The said thermal energy is used in subsequent injections.
    f 0 5 0 d
    five
    0
    five
    sterilizing fluid and allows you to increase the dew point of the mixture by another 10 C.
    Sequential evaporation and thorough mixing, as well as centrifugal action when hot air is injected into the mixing chamber, allows in practice to achieve very efficient evaporation and, as a result, a very high dew point for the resulting mixture. Under optimal conditions, the dew point is only one or several degrees below the theoretical upper limit, which is determined by the thermal air content (usually 60 ° C). The spiral guide serves not only to direct the gas from the inlet to the outlet in order to maintain evaporation more effectively, but also to reduce the noise level during operation.
    权利要求:
    Claims (1)
    [1]
    1. A method of evaporating a sterilizing liquid, mainly hydrogen peroxide, by mixing it with heated air in the chamber, characterized in that, in order to increase efficiency, the air is circulated in a circular spiral trajectory along with the center axis of the spiral movements,
    2, the method according to claim 1, about tliche a ucu and and the fact that the air is supplied in a countercurrent liquid size of 10 -
    80 microns
    I
    3, A device for evaporating a sterilizing liquid, comprising a chamber with inlet and outlet pipes for air and a liquid nozzle, characterized in that the chamber is cylindrical and provided with an internal spiral guide; the outlet of the nozzle is mounted on the end wall of the chamber from the outlet side coaxially with the central axis of the spiral guide passing along the inner lateral surface of the chamber, the inlet and exhaust pipelines being connected to the chamber along a tangent on the ends, and the channel formed
    513860186
    the inner surface of the spiral is 4. The device according to p. 3, t and l is a guide, is made expanding — it is obvious that the channel is in the direction from the nozzle to the entrance apex angle equal to the opening angle of the nozzle.
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    同族专利:
    公开号 | 公开日
    AU2374684A|1984-07-26|
    DE3479192D1|1989-09-07|
    SE8300356L|1984-07-26|
    JPH0524017B2|1993-04-06|
    EP0114619A2|1984-08-01|
    US4512935A|1985-04-23|
    AU566570B2|1987-10-22|
    CA1240613A|1988-08-16|
    JPS59142929A|1984-08-16|
    AT45100T|1989-08-15|
    SE8300356D0|1983-01-25|
    EP0114619B1|1989-08-02|
    EP0114619A3|1987-07-01|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE404480C|1925-01-22|Rappold & Volk A G|Process and device for evaporation of liquids|
    FR377895A|1914-01-16|1907-09-18|James Mecredy|Method and apparatus for drying liquids or semi-liquids|
    US1253766A|1917-04-17|1918-01-15|John L Alden|Dust-separator.|
    DE1035306B|1953-02-26|1958-07-31|Schoppe Fritz|Process for mixing gaseous, liquid or solid substances as well as for the production of reaction products and device for carrying out the process|
    US2817415A|1954-09-01|1957-12-24|Exxon Research Engineering Co|Contacting of fluid phases|
    SE302825B|1965-11-18|1968-08-05|K Rosdahl|
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    US3911642A|1972-09-22|1975-10-14|Tetra Pak Int|Method for the sterile packing of a sterile material|
    US4169123A|1975-12-11|1979-09-25|Moore-Perk Corporation|Hydrogen peroxide vapor sterilization method|
    SE401912B|1976-10-07|1978-06-05|Tetra Pak Int|METHOD OF STERILIZING FOREMS BY LIQUID STERILIZER AND DEVICE FOR IMPLEMENTING THE KIT|
    US4203961A|1978-11-29|1980-05-20|Erco Industries Limited|Chlorine dioxide generation process|
    JPS6215408B2|1979-11-16|1987-04-07|Dainippon Printing Co Ltd|
    DE3125430A1|1981-06-27|1983-01-20|Hick & Co Gmbh, 4901 Hiddenhausen|METHOD AND DEVICE FOR STERILIZING CUP-SHAPED CONTAINERS|DE3540161C2|1985-11-13|1987-08-20|Pkl Verpackungssysteme Gmbh, 4000 Duesseldorf, De|
    JPH0817804B2|1987-12-23|1996-02-28|雪印乳業株式会社|Disinfectant vaporizer|
    WO1990015651A1|1989-06-13|1990-12-27|Aurian Corporation|Method and apparatus for liquid-liquid separation|
    US5258162A|1989-11-07|1993-11-02|Tetra Alfa Holdings S.A.|Method of producing a gaseous hydrogen peroxide-containing sterilization fluid|
    US5176799A|1991-02-28|1993-01-05|Zymark Corporation|Evaporator with solvent recovery feature|
    JP3099200B2|1991-07-15|2000-10-16|四国化工機株式会社|Sterilization method of hydrogen peroxide gas supply device|
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    US6406666B1|2001-02-20|2002-06-18|Tetra Laval Holdings & Finance, Sa|Method and apparatus for vaporizing sterilant hydrogen peroxide|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE8300356A|SE8300356L|1983-01-25|1983-01-25|SET AND DEVICE FOR Vaporizing a liquid|
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