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    • 82. 发明申请
    • FORWARD OSMOSIS SYSTEM COMPRISING SOLVENT SEPARATION BY MEANS OF MEMBRANE DISTILLATION
    • 通过膜分离方法包含溶剂分离的前向OSMOSIS系统
    • US20130264260A1
    • 2013-10-10
    • US13884564
    • 2011-10-06
    • Wolfgang Heinzl
    • Wolfgang Heinzl
    • C02F1/44
    • C02F1/445B01D61/00B01D61/002B01D61/005B01D61/36B01D61/58C02F1/14C02F2103/08C02F2303/16Y02A20/128Y02A20/131
    • The invention relates to a system for separating a product contained as solvent in a solution to be processed, comprising at least one forward osmosis device (816) through which the solution to be processed and a draw solution flow, and a device connected downstream thereof for obtaining the product (56, 62) from the diluted draw solution exiting the forward osmosis device, wherein the forward osmosis device comprises at least one flow channel conducting the solution to be processed and at least one flow channel conducting the draw solution, the inner space of a respective flow channel conducting the solution to be processed is delimited at least partially by a semi-penneable membrane wall that is peimeable to the solvent of the solution to be processed but not to the substance dissolved therein, and at least one flow channel conducting the draw solution is delimited on opposite sides by membrane walls that are associated with two adjoining flow channels conducting the solution to be processed, such that solvent from the solution to be processed passes through the membrane walls into the adjoining flow channels conducting the draw solution.
    • 本发明涉及一种用于分离待处理溶液中作为溶剂的产品的系统,其包括至少一个正向渗透装置(816),待处理溶液和溶液流通过该渗透装置和与其下游连接的装置 从离开正向渗透装置的稀释抽吸溶液获得产物(56,62),其中正向渗透装置包括至少一个导管待处理溶液的流动通道和至少一个传导拉伸溶液的流路,内部空间 进行待处理溶液的相应流动通道的至少部分地由可被待处理溶液的溶剂灼伤但不溶解于其中的物质的半可剥膜膜限定,并且至少一个导流管 拉伸溶液在相对两侧由隔膜壁限定,膜壁与两个相邻的流动通道相连,导通溶液为p 使得来自待处理溶液的溶剂通过膜壁进入导入拉伸溶液的相邻流动通道。
    • 86. 发明申请
    • Forward Osmosis Separation Processes
    • 正向渗透分离过程
    • US20120228222A1
    • 2012-09-13
    • US13420052
    • 2012-03-14
    • Robert L. McGinnisMenachem Elimelech
    • Robert L. McGinnisMenachem Elimelech
    • B01D61/36B01D61/00
    • C02F1/445B01D61/002B01D61/005B01D61/36C02F1/02C02F2103/08Y02A20/131Y02W10/37
    • Separation processes using forward osmosis are disclosed generally involving the extraction of a solvent from a first solution to concentrate a solute therein by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. One or both of the solute and solvent may be a desired product. By manipulating the equilibrium of the soluble and insoluble species of solute within the second solution, a saturated second solution can be used to generate osmotic pressure on the first solution. The various species of solute within the second solution can be recovered and recycled through the process to affect the changes in equilibrium and eliminate waste products. Enhanced efficiency may result from using low grade waste heat from industrial or commercial sources.
    • 公开了使用正向渗透的分离方法,其通常涉及通过使用第二浓缩溶液从第一溶液中提取溶剂以从第一溶液中萃取溶质以浓缩其中的溶液,以通过半透膜从第一溶液中抽出溶剂。 溶质和溶剂中的一种或两种可以是所需的产物。 通过操纵第二溶液中可溶性和不溶性溶质物质的平衡,可以使用饱和的第二溶液在第一溶液上产生渗透压。 第二溶液中的各种溶质可以通过该过程回收和回收,以影响平衡的变化并消除废物。 使用工业或商业来源的低品位废热可能会提高效率。
    • 87. 发明申请
    • Osmotic Desalination Process
    • 渗透脱盐工艺
    • US20120091062A1
    • 2012-04-19
    • US13086050
    • 2011-04-13
    • Robert L. McGinnis
    • Robert L. McGinnis
    • C02F1/44
    • B01D61/002B01D61/005C02F1/02C02F1/44C02F1/445C02F2103/08Y02A20/131Y02W10/33Y02W10/37
    • An energy efficient desalination process that does not produce waste products involves the extraction of water from a first solution, such as seawater, by using a second concentrated solution to draw the water from the first solution across a semi-permeable membrane. By manipulating the equilibrium of the soluble and insoluble species of solute within the second solution in favor of the soluble species of the solute, a saturated second solution can be used to generate osmotic pressure on the first solution. Also, by adjusting the equilibrium in favor of the less soluble species after the water has been drawn from the first solution, a portion of the solute can easily be precipitated out. Heating the second solution decomposes the solute into its constituent gases. The constituent gases and precipitated solute may be recycled through the process to affect the changes in equilibrium and eliminate waste products. Additionally, by using the waste steam from industrial sources and a heat pump to effectively distribute heat through the present method, the present method exhibits greater energy efficiency than prior art methods.
    • 不产生废物的能量高效脱盐方法涉及通过使用第二浓缩溶液从第一溶液中通过半透膜抽出水从第一溶液(例如海水)中提取水。 通过操纵第二溶液中可溶性和不溶性溶质的平衡,有利于溶质的可溶性物质,可以使用饱和的第二溶液在第一溶液上产生渗透压。 此外,通过在从第一溶液中抽出水后,通过调节有利于较少溶解物质的平衡,溶质的一部分可以容易地沉淀出来。 加热第二溶液将溶质分解成其组成气体。 组分气体和沉淀溶质可以通过该过程再循环,以影响平衡的变化并消除废物。 此外,通过使用来自工业源的废蒸汽和热泵通过本方法有效地分配热量,本方法比现有技术方法显示出更大的能量效率。