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    • 5. 发明申请
    • CYCLONIC EVAPORATOR
    • 循环蒸发器
    • WO00018483A1
    • 2000-04-06
    • PCT/AU1999/000836
    • 1999-09-30
    • B01D3/08B01D19/00B04C3/02B04C3/04B04C3/06B04C5/06B04C5/20B04C5/28B04C9/00B01D1/00
    • B01D3/08B01D19/0057B04C3/02B04C3/04B04C3/06B04C5/06B04C5/20B04C5/28B04C9/00
    • A method and apparatus for separating the components of a feed material prior to or simultaneously with at least partially vaporising one of the components is described. The apparatus comprises at least one inlet (8) for admitting the feed material (10) containing the two components to the apparatus (2) wherein a device for introducing a first movement to the feed material is located, such as, for example, an in-line swirl generator (14), which imparts a swirling movement to the feed material to partially separate the components into two swirling flows. The partially separated material on emerging from the in-line swirl generator (14) is in an evaporation tube (20) in which the more volatile component is vaporised to further assist in separating the two components into a liquid component and a gaseous or vapour component. The liquid component and the vapour phase are discharged from the apparatus in two streams through the same outlet (36). Modifications of the method and apparatus include (i) having multiple evaporation tubes (20), each optionally provided with its own in-line swirl generator to facilitate better distribution and separation of the feed material, and (ii) having a reject nozzle (40) and reject conduit (42) located within the generator for allowing passage of vapour or gas through the in-line swirl generator (14) when there is an intermediate flow formed in the generator (14) and conveyed to the evaporation tube (20). The method and apparatus of this application are used as a pre-treatment in an overall separation plant.
    • 描述了在至少部分蒸发其中一个部件之前或同时分离进料的组分的方法和装置。 所述装置包括至少一个入口(8),用于将包含两个部件的进料(10)进入装置(2),其中用于将第一运动引入给料材料的装置位于,例如, 在线旋流发生器(14),其向进给材料施加旋转运动以部件将部件分离成两个旋流。 从直列涡流发生器(14)出来的部分分离的材料在蒸发管(20)中,其中挥发性较高的组分被蒸发以进一步有助于将两种组分分离成液体组分和气体或蒸汽组分 。 液体组分和气相通过相同的出口(36)以两股流从设备排出。 该方法和设备的修改包括(i)具有多个蒸发管(20),每个蒸发管可选地设置有自己的直列旋流发生器,以便于进料的更好的分配和分离,和(ii)具有排出喷嘴 )并且当存在形成在发电机(14)中的中间流并被输送到蒸发管(20)时,位于发电机内的导管(42)被允许蒸气或气体通过直列旋流发生器(14) 。 本申请的方法和装置用作整个分离装置中的预处理。
    • 7. 发明申请
    • VERFAHREN UND ANORDNUNG ZUR ABGASREINIGUNG BEI VAKUUM-STAHLBEHANDLUNGSPROZESSEN
    • 方法和系统排放在真空中钢TREATMENT用
    • WO2013110647A1
    • 2013-08-01
    • PCT/EP2013/051224
    • 2013-01-23
    • INTECO SPECIAL MELTING TECHNOLOGIES GMBH
    • LUVEN, MichaelOBITZ, JohannesLUVEN, Arno
    • B04C5/12B04C5/15B04C5/20B04C9/00
    • B04C9/00B01D45/12B01D46/4263B01D50/002B04C5/12B04C5/15B04C5/20B04C2009/004
    • Die Erfindung betrifft ein Verfahren zur Abgasreinigung bei Entgasungsanlagen unter Verwendung einer Einrichtung (16) zur Erzeugung eines Unterdrucks, insbesondere mittels Dampfstrahl-Ejektorpumpen oder mechanischen Vakuumpumpen. Erfindungsgemäß ist es vorgesehen, dass das von einem Rezipienten (15) kommende Abgas in einen Zyklonabscheider (12) geleitet wird, und dass die Verfahrensschritte Grobabscheidung von Partikeln aus dem Abgas und Feinstaubabscheidung von Partikeln aus dem Abgas sowie Gaskühlung in dem Zyklonabscheider (12) hintereinander in der Weise durchgeführt werden, dass das Abgas nach erfolgter Grobreinigung direkt über einen im Zyklonabscheider (12) eingebauten Feinstaubfilter (13) und anschließend durch einen an den Feinstaubfilter (13) sich anschließenden Gaskühler (14) in eine mit der Einrichtung (16) zur Erzeugung eines Unterdrucks verbundene Saugleitung (2) zur Einrichtung (16) geführt wird.
    • 本发明涉及一种用于净化废气用于使用的装置(16),用于通过蒸汽射流喷射器或机械真空泵装置产生真空,特别是脱气的方法。 根据本发明,它提供的是,接收方(15)来的废气被通入旋风分离器(12),以及在于该方法步骤从排气颗粒和从废气中细微尘粒和气体在旋风分离器冷却的粗分离在另一个后面(12)一个 以这样的方式,所述粗清洗之后的废气直接内置通过在旋风分离器(12)细尘接着是在所述颗粒物过滤器(13)邻接在一个与所述装置(16),气体冷却器(14)的过滤器(13)来进行 产生负连接到所述抽吸管线(2),用于装置(16)的压力被引导。
    • 8. 发明申请
    • CYCLONE DISTILLERY/REFINERY HAVING STEAM DUCTED IMPELLER/TURBINE
    • 具有蒸汽导向叶轮/涡轮机的循环蒸馏器/精炼机
    • WO2012177157A1
    • 2012-12-27
    • PCT/RS2011/000010
    • 2011-06-28
    • PERUNICIC, Dragoljub
    • PERUNICIC, DragoljubPERUNICIC, Darko
    • B01D3/00B04C5/04B04C5/20B01D5/00
    • B01D3/00B01D3/004B01D5/0024
    • The distillation-power unit (4) of a distillery/refinery (1) consists of a radial flow steam driven ducted impeller (71) which is driven by steam released from bubbles coming on the surface of liquid for distillation contained in a cyclone conical container (13, 70) and multi-stage axial flow bubble driven ducted impeller (72) which is driven by bubbles of saturated steam ascending from the heated bottom of container (13, 70). The steam and bubble driven impeller (71, 72) are fixed to an outer and inner vertical shaft (75, 76) of induction generator/motor (7) respectively. Exhaust steam is condensed inside the top cap/fan casing (10) of steam driven impeller (72). Vapor from the cap/fan casing (10) is delivered to the condensation unit (5) where it is condensed into fuel for supplying a burner which burns fuel and heats the bottom of container (70). Non-condensed gases returns into the distillation-power unit (4).
    • 蒸馏器/精炼厂(1)的蒸馏功率单元(4)由径向流动蒸汽驱动的管道叶轮(71)组成,该叶轮被从蒸发液体中释放的蒸汽驱动,该气体包含在旋风锥形容器 (13,70)和多级轴流气泡驱动管道叶轮(72),其由从容器(13,70)的加热底部上升的饱和蒸汽气泡驱动。 蒸汽和气泡驱动的叶轮(71,72)分别固定在感应发电机/电动机(7)的外部和内部垂直轴(75,76)上。 排气蒸汽在蒸汽驱动叶轮(72)的顶盖/风扇壳体(10)内冷凝。 来自盖/风扇壳体(10)的蒸汽被输送到冷凝单元(5),在该冷凝单元(5)处被冷凝成燃料以供应燃烧燃料的燃烧器并加热容器(70)的底部。 非冷凝气体返回蒸馏功率单元(4)。
    • 10. 发明申请
    • HEATING AND INCINERATION DEVICE
    • 加热和焚烧装置
    • WO00009949A1
    • 2000-02-24
    • PCT/US1999/017355
    • 1999-07-30
    • F23G5/50B04C5/13B04C5/14B04C5/20B04C9/00F23G7/06F23J17/00F23G5/32
    • F23G7/065A23N12/125
    • A heating and incineration device includes a heating chamber (15) for being connected to a heating application (17). A process stream is recirculated between the heating chamber and the heating application. An incineration tube (22) is positioned into the heating chamber for providing the only exit for gases from the heating chamber and the heating application. A heat source (11) is positioned within the heating chamber in spaced coaxial relation with an incineration tube inlet. The process stream is heated to a working temperature when it is passed through the heating chamber around the periphery of the heat source. The heat source is directed at the incineration tube inlet, so that the highest temperature inside the heating chamber is concentrated along an axis between the heat source and the incineration tube inlet. The distance between the incineration tube inlet and the heat source is adjustable for controlling the temperature inside the incineration tube. Pollutants in the exhaust gases flowing out through the incineration tube are incinerated by the very high temperature inside the tube. Energy efficiency is thus significantly increased by recirculating the process stream, by exhausting a small amount of gases, and by heating the process stream and incinerating pollutants with a single heat source.
    • 加热和焚烧装置包括用于连接到加热应用(17)的加热室(15)。 工艺流在加热室和加热应用之间循环。 焚烧管(22)位于加热室中,用于仅提供来自加热室和加热应用的气体出口。 热源(11)以与焚烧管入口间隔的同轴关系位于加热室内。 当工艺物流通过加热室周围的热源时被加热到工作温度。 热源指向焚烧管入口,使得加热室内的最高温度沿着热源和焚烧管入口之间的轴线集中。 焚烧管入口和热源之间的距离是可调节的,用于控制焚烧管内的温度。 通过焚烧管流出的废气中的污染物被管内非常高的温度焚烧。 因此,通过再循环工艺流,排出少量气体以及通过加热工艺流并用单个热源焚烧污染物,能量效率显着提高。