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    • 1. 发明申请
    • Convenient Substance-Recovery System and Process
    • 方便的物质回收系统和工艺
    • US20090071334A1
    • 2009-03-19
    • US12139817
    • 2008-06-16
    • Jae Ryu
    • Jae Ryu
    • B01D53/04
    • H01M8/0618B01D53/228B01D69/02B01D69/10B01D2323/225B01D2325/36H01M8/04119H01M8/04171
    • A polar-substance-permselective membrane includes a porous support and an active-membrane material. The active-membrane material fills the pores of the porous support to render the support substantially impermeable to non-polar gases at a moderate pressure gradient (e.g., at least 70 kPa) when the hydrophilic active-membrane material is wet. In a particular embodiment the membrane is water-permselective and the active-membrane material is hydrophilic. Water-recovery system and processes utilizing these water-permselective membranes can be used to selectively remove water from hot gas streams at the feed side, and collect water at the permeate side with extremely high energy efficiency. The membrane is particularly useful for in-situ extraction of water molecules directly from hot exhaust streams. The produced steam, or steam and air mixtures can be used as a feedstock in the process of converting liquid hydrocarbons into hydrogen-rich gas streams.
    • 极性物质选择性渗透膜包括多孔载体和活性膜材料。 当亲水性活性膜材料是湿的时,活性膜材料填充多孔载体的孔,使得支撑体在中等压力梯度(例如至少70kPa)下基本上不渗透非极性气体。 在一个具体实施方案中,膜是水选择性选择性的,并且活性膜材料是亲水的。 利用这些水选择性渗透膜的水回收系统和方法可以用于选择性地从进料侧的热气流中除去水,并以极高的能量效率在渗透侧收集水。 该膜特别适用于直接从热排气流中原位萃取水分子。 在将液体烃转化为富氢气流的过程中,所产生的蒸汽或蒸气和空气混合物可用作原料。