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    • 3. 发明授权
    • Apparatus and process for selectively removing a component from a
multicomponent aqueous solution by pervaporation
    • 通过渗透蒸发从多组分水溶液中选择性地除去组分的装置和方法
    • US5993515A
    • 1999-11-30
    • US972437
    • 1997-11-18
    • Kamalesh K. Sirkar
    • Kamalesh K. Sirkar
    • B01D61/36B01D69/08B01D69/12C02F1/44B01D19/00B01D53/22
    • B01D61/362B01D69/08B01D69/12B01D69/127C02F1/44C02F1/444C02F1/448
    • A pervaporation process for selectively removing a component from a multicomponent aqueous solution which is practiced with an assembly comprising a feed chamber for holding and introducting the multicomponent aqueous solution to be treated therein, the feed chamber having a pressure, an exit chamber having a pressure, and located adjacent to the feed chamber and downstream thereof; at least one membrane composite located between the feed chamber and the exit chamber and adapted for fluid registry therewith, the membrane composite comprised of a porous membrane having a first and second surface, and a nonporous membrane permanently disposed on the second surface of the porous membrane, and having a permeability selective to the component, the membrane composite aligned such that the nonporous membrane is connected to the feed chamber; and a vacuum pump connected to the exit chamber for evacuating the component from the chamber. The process comprises the steps of introducing the multicomponent aqueous solution into the feed chamber, evacuating the component from the exit chamber, so that the pressure in the exit chamber is less than the pressure in the feed chamber, contacting the multicomponent aqueous solution with the first surface of the porous membrane.
    • 一种用于选择性地从多组分水溶液中除去组分的渗透蒸发方法,该组合物包括用于保持和引入待处理的多组分水溶液的进料室,所述进料腔具有压力,具有压力的出口室, 并且位于邻近进料室并在其下游; 至少一个膜复合材料位于进料室和出口室之间并且适于与其流体对准,所述膜复合物由具有第一和第二表面的多孔膜和永久地设置在多孔膜的第二表面上的无孔膜组成 并且具有对组分选择性的渗透性,所述膜复合物对齐,使得所述无孔膜连接到所述进料室; 以及连接到出口室的真空泵,用于将部件从腔室排出。 该方法包括以下步骤:将多组分水溶液引入进料室,将组分从出口室排出,使得出口室中的压力小于进料室中的压力,使多组分水溶液与第一 多孔膜的表面。
    • 4. 发明授权
    • Immobilized-interface solute-transfer apparatus
    • 固定界面溶质转移装置
    • US4789468A
    • 1988-12-06
    • US644895
    • 1984-08-28
    • Kamalesh K. Sirkar
    • Kamalesh K. Sirkar
    • B01D11/04B01D61/24B01D61/28B01D61/32B01D63/04B01D13/00
    • B01D61/246B01D11/0415B01D61/28B01D61/32B01D63/043B01D2313/50
    • An immobilized-interface solute-transfer unit for transferring solute from a feed solution to an extractant liquid comprises a fluid-tight housing and a porous membrane which divides the housing into a feed solution chamber and an extractant chamber. The housing has feed solution inlet and outlet ports which communicate with the feed solution chamber, and extractant inlet an outlet ports which communicate with the extractant chamber. The solute-transfer unit also includes a presure difference controller for maintaining a difference between a liquid pressure of a feed solution in the feed solution chamber and a liquid presure of an extractant in the extractant chamber substantially within a predetermined pressure range so that an interface between the feed solution and the extractant is substantially immobilized at the membrane. The solute-transfer unit is particularly adapted for transferring a solute from a feed solution to an extractant, which feed solution and extractant are immiscible with one another when in direct contact.
    • 用于将溶质从进料溶液输送到萃取剂液体的固定界面溶质转移单元包括流体密封壳体和将壳体分成进料溶液室和萃取室的多孔膜。 壳体具有与进料溶液室连通的进料溶液入口和出口,萃取剂入口与萃取室连通。 溶质转移单元还包括压差差值控制器,用于保持进料溶液室中的进料溶液的液体压力与萃取剂室中的萃取剂的液体压力之间的差异,基本上在预定压力范围内, 进料溶液和萃取剂基本上固定在膜上。 溶质转移单元特别适于将溶质从进料溶液转移到萃取剂中,该进料溶液和萃取剂在直接接触时彼此不混溶。
    • 5. 发明授权
    • Selective-permeation gas-separation process and apparatus
    • 选择性渗透气体分离方法及装置
    • US4750918A
    • 1988-06-14
    • US738793
    • 1985-05-28
    • Kamalesh K. Sirkar
    • Kamalesh K. Sirkar
    • B01D53/22B01D61/38
    • B01D61/38B01D53/22B01D53/229B01D2251/304B01D2251/306B01D2251/606B01D2252/10B01D2252/20484B01D2252/20489B01D2256/245B01D2257/304B01D2257/502B01D2257/504B01D2258/05B01D2317/08B01D2319/06B01D53/1493Y02C10/10
    • A permeant gas is selectively transferred from a feed-gas mixture which comprises the permeant gas and at least one other component to an output fluid by the process of the invention. The process involves introducing a selective-permeation liquid into a permeation-transfer chamber. A gas-depletion channel and a gas-enrichment channel pass through the permeation chamber and are separated from the chamber respectively by porous walls. The selective-permeation liquid contacts the porous walls but does not flow into the gas-depletion or gas-enrichment channels. The feed-gas mixture is introduced into the gas-depletion channel so that permeant gas in the mixture can pass through the pores of the walls of the channel into the selective-permeation liquid and from the selective-permeation liquid through the pores of the walls of the gas-enrichment channel into the gas-enrichment channel. Permeant gas is withdrawn from the gas-enrichment channel and a stream of gas depleted in the permeant gas is withdrawn from the gas-depletion channel. A gas-transfer unit permits the process of the invention to be carried out effectively.
    • 通过本发明的方法,将渗透气体从包含透过气体和至少一种其它组分的进料 - 气体混合物中选择性转移到输出流体。 该方法包括将选择性渗透液体引入渗透转移室。 气体耗尽通道和气体富集通道穿过渗透室并分别通过多孔壁与腔室分离。 选择性渗透液体接触多孔壁,但不流入气体消耗或气体浓缩通道。 将进料 - 气体混合物引入气体消耗通道中,使得混合物中的渗透气体可以通过通道壁的孔进入选择性渗透液体,并从选择性渗透液体通过壁的孔 的气体富集通道进入气体浓缩通道。 从气体富集通道排出渗透气体,并且从气体消耗通道中排出贫化的渗透气体中的气体流。 气体传递单元允许有效地执行本发明的方法。
    • 9. 发明授权
    • Desalination devices and systems using porous hydrophobic hollow fibers and hydrophobic porous coatings
    • 使用多孔疏水中空纤维和疏水多孔涂层的海水淡化装置和系统
    • US08167143B2
    • 2012-05-01
    • US11189213
    • 2005-07-26
    • Kamalesh K. SirkarBaoan Li
    • Kamalesh K. SirkarBaoan Li
    • B01D63/02B01D61/36B01D61/00
    • B01D61/364B01D63/02B01D63/026B01D67/0088B01D69/02B01D69/08Y02A20/131
    • DCMD and VMD systems and methods for use in desalination applications are provided. The DCMD and VMD systems employ coated porous hydrophobic hollow fiber membranes. The coatings advantageously function to essentially eliminate pore wetting of the membrane, while permitting substantially unimpeded water vapor permeance through the fiber walls. The DCMD and VMD membranes are characterized by larger fiber bore diameters and wall thicknesses. The membranes substantially reduce the loss of brine sensible heat, e.g., heat loss via conductive heat flux through the membrane wall and the vapor space and, in exemplary embodiments, the brine-side heat transfer coefficient is dramatically enhanced by horizontal/vertical cross flow of brine over the outside surface of the coated fibers. Superior water vapor fluxes are achieved with the systems and methods.
    • 提供了用于脱盐应用的DCMD和VMD系统和方法。 DCMD和VMD系统采用涂覆的多孔疏水性中空纤维膜。 涂层有利地基本上消除了膜的毛孔润湿,同时允许通过纤维壁的基本上无阻碍的水蒸气渗透。 DCMD和VMD膜的特征在于较大的纤维孔直径和壁厚。 膜基本上减少了盐水显热的损失,例如通过膜壁和蒸汽空间的导热热通量的热损失,并且在示例性实施例中,盐水侧传热系数通过水平/垂直横流 盐水在涂覆纤维的外表面上。 通过系统和方法实现了卓越的水汽通量。