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    • 5. 发明授权
    • Process for the enrichment of gases
    • 气体浓缩过程
    • US4011065A
    • 1977-03-08
    • US523687
    • 1974-11-14
    • Heinrich MunznerHeinrich HeimbachWerner KorbacherWerner PetersHarald JuntgenKarl KnoblauchDieter Zundorf
    • Heinrich MunznerHeinrich HeimbachWerner KorbacherWerner PetersHarald JuntgenKarl KnoblauchDieter Zundorf
    • B01D53/04C01B13/02B01D15/06
    • B01D53/0423B01D53/04C01B13/0266B01D2253/102B01D2256/12B01D2259/402B01D53/0446C01B2210/0046
    • An initial gaseous mixture of at least two components is passed through an adsorber which preferentially adsorbs one of the components. This initially loads the adsorber. Subsequently, another gaseous mixture, having a greater concentration of the preferentially adsorbed component than the initial gaseous mixture, is passed through the adsorber so as to additionally load the adsorber. Part of the gas in the adsorber is then removed. This initially unloads the adsorber and yields a first fraction containing both components with the concentration of the preferentially adsorbed component being greater than that in the initial gaseous mixture. Subsequently, part of the gas still remaining in the adsorber is removed so as to further unload the adsorber. This results in a second fraction including both components and wherein the concentration of the preferentially adsorbed component is greater than that in both the second gaseous mixture to be passed through the adsorber and the first fraction removed from the adsorber. Finally, the remainder of the gas in the adsorber is removed so as to completely unload the adsorber. This yields a third fraction including both components with the concentration of the preferentially adsorbed component being lower than that in the second fraction removed from the adsorber but greater than that in the initial gaseous mixture passed into the adsorber. The first and third fractions may be used for additionally loading the adsorber in a subsequent cycle. A preferred application is the enrichment of oxygen-containing gases, particularly air, which include a component of greater molecular size than oxygen. A preferred adsorber is molecular sieve coke which preferentially adsorbs the oxygen. The process permits air to be enriched to such an extent that the product fraction, namely, the second fraction, removed from the adsorber contains between 70 and 95 volume percent of oxygen.
    • 9. 发明授权
    • Method and apparatus for thermal treatment, especially drying, of finely
comminuted bulk material
    • 用于热处理,特别是干燥的细粉碎散装材料的方法和装置
    • US4439932A
    • 1984-04-03
    • US479110
    • 1983-03-28
    • Gunther GappaJosef DegelHarald Juntgen
    • Gunther GappaJosef DegelHarald Juntgen
    • B01J8/38F26B3/00F26B3/084F26B3/092F26B11/14F26B25/04F26B17/10
    • F26B3/084F26B25/04F26B3/00F26B3/092
    • A method for thermal treatment, especially drying, of finely particulated bulk material comprises the steps of stirring the material in a reactor by means of a rotating stirrer while simultaneously discharging a heated gas under pressure through openings in a hollow arm of the stirrer so as to form in the reactor a whirling fluidized bed from the material, and introducing the necessary amount of heat for the thermal treatment of the material at least in part through a heat exchanger extending into the whirling fluidized bed. The apparatus for carrying out the method mainly comprises an arrangement for feeding the material through an inlet into a reactor forming a whirling chamber in which a rotating stirring device is arranged having at least one hollow stirring arm provided with openings through which a preferably heated gas under pressure is discharged into the material so as to form a whirling fluidized bed in the reactor, a heat exchanger extending through the fluidized bed, and an outlet for discharging the gas and treated material from the reactor. The reactor may also include an arrangement extending into the whirling fluidized bed for retarding flow of the material from the inlet to the outlet of the reactor, which arrangement may be constituted by a heat exchanger of lamellar construction so that the material will pass in cascades through the reactor.
    • 用于热处理,特别是干燥的细颗粒体积材料的方法包括以下步骤:通过旋转搅拌器在反应器中搅拌材料,同时通过搅拌器的空心臂中的开口在压力下排出加热气体,从而 在反应器中形成来自材料的旋转流化床,并且通过延伸到旋转流化床的热交换器至少部分地引入必要量的热量用于材料的热处理。 用于执行该方法的装置主要包括一种用于将材料通过入口供入到形成旋转室的反应器的装置,其中设置有旋转的搅拌装置,其具有设置有开口的至少一个中空搅拌臂,通过该开口, 压力被排出到材料中,以便在反应器中形成旋转流化床,延伸穿过流化床的热交换器和用于从反应器排出气体和处理材料的出口。 反应器还可以包括延伸到旋转流化床中的装置,用于阻止材料从反应器的入口到出口的流动,该布置可以由层状结构的热交换器构成,使得材料级联通过 反应堆。