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    • 6. 发明申请
    • MEMBRANE DISTILLATION SYSTEM AND METHOD
    • 膜分离系统和方法
    • US20110180383A1
    • 2011-07-28
    • US12694757
    • 2010-01-27
    • Zidu MaTimothy D. DavisJames R. IrishGary D. Winch
    • Zidu MaTimothy D. DavisJames R. IrishGary D. Winch
    • B01D61/36B01D3/00C02F1/04
    • B01D61/364B01D63/02B01D2313/38F28D21/0015Y02W10/37
    • A membrane distillation system includes a distillation vessel, an array of hollow fiber membranes pervious to distillate vapor but impervious to feed solution and an array of hollow tubes impervious to distillate vapor and feed solution but which allow thermal energy transmission. The system further includes a pump, a heat exchanger for heating the feed solution before it enters the hollow fiber membranes, and an outlet for removing distillate from the distillation vessel. A method for removing distillate from a feed solution includes delivering the feed solution through hollow tubes spanning a distillation vessel, heating the feed solution, delivering the feed solution through hollow fiber membranes spanning the distillation vessel to create a vapor pressure differential between the hollow fiber membranes and a distillation volume within the distillation vessel, and removing distillate from the distillation vessel.
    • 膜蒸馏系统包括蒸馏容器,可透过蒸馏物蒸气但不能进料溶液的中空纤维膜阵列,以及不透水蒸馏和进料溶液但允许热能传递的中空管阵列。 该系统还包括泵,用于在进料溶液进入中空纤维膜之前加热进料溶液的热交换器,以及用于从蒸馏容器除去馏出物的出口。 从进料溶液中除去馏出物的方法包括将进料溶液通过跨越蒸馏容器的中空管输送,加热进料溶液,通过跨越蒸馏容器的中空纤维膜输送进料溶液以在中空纤维膜之间产生蒸气压差 和蒸馏容器内的蒸馏体积,并从蒸馏容器中除去馏出物。
    • 7. 发明申请
    • Membrane distillation pressure control system and method
    • 膜蒸馏压力控制系统及方法
    • US20100065496A1
    • 2010-03-18
    • US12283597
    • 2008-09-12
    • Zidu MaXiaohong LiaoJames R. Irish
    • Zidu MaXiaohong LiaoJames R. Irish
    • B01D61/36
    • B01D61/364B01D2311/10B01D2311/14B01D2313/083
    • A membrane distillation system includes a membrane distillation module, a brine loop and a distillate loop. The brine loop and the distillate loop each include means for regulating flow of brine solution and distillate, respectively, to the membrane distillation module. The flow of brine solution and distillate is regulated to prevent brine solution and distillate from penetrating membranes of the membrane distillation module. A method of membrane distillation includes delivering brine solution and distillate to the membrane distillation module at low pressures in a first mode. The method also includes heating the brine solution and cooling the distillate and delivering portions of each to the membrane distillation module in a second mode. The portions of heated brine solution and cooled distillate are adjusted to facilitate membrane distillation while preventing liquid from penetrating membranes of the membrane distillation module.
    • 膜蒸馏系统包括膜蒸馏模块,盐水回路和馏出物回路。 盐水回路和馏出物回路各自包括用于将盐水溶液和馏出物分别调节到膜蒸馏模块的装置。 调节盐水溶液和馏出物的流动,以防止盐水溶液和蒸馏物渗透膜蒸馏模块的膜。 膜蒸馏的方法包括在第一模式中以低压将盐水溶液和馏出物输送到膜蒸馏模块。 该方法还包括加热盐水溶液并冷却馏出物并以第二模式将各部分输送到膜蒸馏模块。 调节加热的盐水溶液和冷却的馏出物的部分以促进膜蒸馏,同时防止液体渗透膜蒸馏模块的膜。
    • 9. 发明申请
    • HEAT EXCHANGE SYSTEM CONFIGURED WITH A MEMBRANE CONTACTOR
    • 配有膜接触器的热交换系统
    • US20130206658A1
    • 2013-08-15
    • US13372121
    • 2012-02-13
    • Hailing WuZidu Ma
    • Hailing WuZidu Ma
    • B01D29/00
    • B01D3/007C02F1/16F24T10/00F28C3/08F28D15/0266F28D21/0001F28D21/0015Y02E10/10Y02W10/37
    • A heat exchange system may include a first heat exchange circuit and a second heat exchange circuit. The first heat exchange circuit may circulate a first working fluid sequentially through a first heat exchanger, a second heat exchanger and a membrane contactor. The second heat exchange circuit may direct a second working fluid sequentially through the first heat exchanger and the membrane contactor, where the second working fluid includes solute and solvent. The first heat exchanger and the membrane contactor may transfer heat energy from the second working fluid to the first working fluid, and the second heat exchanger may transfer heat energy from the first working fluid to a third working fluid. The membrane contactor may extract a portion of the solvent from the second working fluid.
    • 热交换系统可以包括第一热交换电路和第二热交换电路。 第一热交换回路可以顺序地通过第一热交换器,第二热交换器和膜接触器循环第一工作流体。 第二热交换回路可以使第二工作流体依次通过第一热交换器和膜接触器,其中第二工作流体包括溶质和溶剂。 第一热交换器和膜接触器可以将热能从第二工作流体传递到第一工作流体,并且第二热交换器可以将热能从第一工作流体传递到第三工作流体。 膜接触器可以从第二工作流体中提取一部分溶剂。