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    OSMOTICALLY DRIVEN MEMBRANE PROCESSES AND SYSTEMS AND METHODS FOR DRAW SOLUTE RECOVERY
    1.
    发明申请
    OSMOTICALLY DRIVEN MEMBRANE PROCESSES AND SYSTEMS AND METHODS FOR DRAW SOLUTE RECOVERY 审中-公开
    动态驱动膜过程和系统及其解决方案

    公开(公告)号：WO2012040335A3

    公开(公告)日：2012-07-05

    申请号：PCT/US2011052565

    申请日：2011-09-21

    申请人： OASYS WATER INC ,  MCGINNIS ROBERT

    发明人： MCGINNIS ROBERT

    IPC分类号： B01D61/10 ,  B01D61/02 ,  B01D61/06

    CPC分类号： B01D61/002 ,  B01D61/364 ,  B01D2311/26 ,  B01D2311/2626 ,  B01D2311/2669 ,  B01D2313/36 ,  Y02W10/33 ,  Y02W10/37

    摘要： The invention relates to osmotically driven membrane processes and systems and methods for recovering draw solutes in the osmotically driven membrane processes. Osmotically driven membrane processes involve the extraction of a solvent from a first solution to concentrate solute by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. Draw solute recovery may be carried out by various means including with the use of a membrane device. The draw solute recovery may also include the use of multi-stage solute recovery using distillation columns and/or membranes, where the recovery may be assisted by a heat pump.

    摘要翻译： 本发明涉及渗透驱动的膜方法和用于在渗透驱动的膜过程中回收牵伸溶质的系统和方法。 渗透驱动的膜方法包括通过使用第二浓缩溶液从第一溶液中萃取溶剂以浓缩溶质，以通过半透膜从第一溶液中抽出溶剂。 可以通过包括使用膜装置的各种手段进行溶质回收。 拉伸溶质回收还可以包括使用使用蒸馏塔和/或膜的多阶段溶质回收，其中回收可以由热泵辅助。

    OSMOTICALLY DRIVEN MEMBRANE PROCESSES AND SYSTEMS AND METHODS FOR DRAW SOLUTE RECOVERY
    3.
    发明申请
    OSMOTICALLY DRIVEN MEMBRANE PROCESSES AND SYSTEMS AND METHODS FOR DRAW SOLUTE RECOVERY 审中-公开
    渗透驱动膜过程和系统以及绘制溶质回收的方法

    公开(公告)号：WO2012040335A2

    公开(公告)日：2012-03-29

    申请号：PCT/US2011/052565

    申请日：2011-09-21

    申请人： OASYS WATER, INC. ,  MCGINNIS, Robert

    发明人： MCGINNIS, Robert

    IPC分类号： B01D61/10 ,  B01D61/06 ,  B01D61/02

    CPC分类号： B01D61/002 ,  B01D61/364 ,  B01D2311/26 ,  B01D2311/2626 ,  B01D2311/2669 ,  B01D2313/36 ,  Y02W10/33 ,  Y02W10/37

    摘要： The invention relates to osmotically driven membrane processes and systems and methods for recovering draw solutes in the osmotically driven membrane processes. Osmotically driven membrane processes involve the extraction of a solvent from a first solution to concentrate solute by using a second concentrated solution to draw the solvent from the first solution across a semi-permeable membrane. Draw solute recovery may be carried out by various means including with the use of a membrane device. The draw solute recovery may also include the use of multi-stage solute recovery using distillation columns and/or membranes, where the recovery may be assisted by a heat pump.

    摘要翻译： 本发明涉及用于回收渗透驱动的膜过程中的驱动溶质的渗透驱动的膜过程和系统和方法。 渗透驱动的膜过程涉及从第一溶液中提取溶剂以通​​过使用第二浓缩溶液浓缩溶质以从第一溶液中将溶剂从半渗透膜中抽出。 抽取溶质回收可以通过各种方式进行，包括使用膜装置。 汲取溶质回收还可包括使用蒸馏塔和/或膜的多阶段溶质回收，其中回收可通过热泵辅助。

    DETERMINING BIOFILM THICKNESS IN A MEMBRANE SUPPORTED BIOFILM REACTOR
    5.
    发明申请
    DETERMINING BIOFILM THICKNESS IN A MEMBRANE SUPPORTED BIOFILM REACTOR 审中-公开
    在薄膜支持的生物反应器中测定生物膜厚度

    公开(公告)号：WO2010061365A1

    公开(公告)日：2010-06-03

    申请号：PCT/IE2009/000081

    申请日：2009-11-25

    申请人： UNIVERSITY COLLEGE DUBLIN, NATIONAL UNIVERSITY OF IRELAND, DUBLIN ,  CASEY, Eoin ,  SYRON, Eoin ,  HEFFERNAN, Barry

    发明人： CASEY, Eoin ,  SYRON, Eoin ,  HEFFERNAN, Barry

    IPC分类号： G01B13/06 ,  C02F3/12

    CPC分类号： C02F3/006 ,  B01D61/10 ,  B01D61/12 ,  B01D63/02 ,  B01D65/02 ,  B01D65/10 ,  B01D69/08 ,  B01D2311/14 ,  B01D2311/16 ,  B01D2311/26 ,  B01D2321/18 ,  B01D2321/40 ,  C02F3/102 ,  G01B13/06 ,  Y02W10/15

    摘要： A method of assessing biofilm thickness in a membrane supported biofilm reactor (MSBR) of the type comprising a lumen containing a gas phase, a liquid phase, and a gas permeable membrane providing an interface between the gas and liquid phases, the method comprising the steps of charging the lumen with an inert gas, closing the lumen to establish an initial elevated pressure in the lumen, measuring the rate of change of pressure within the lumen, and correlating the rate of change of pressure (dP/dt) with biofilm thickness. The step of correlating dP/dt with biofilm thickness involves correlating dP/dt with the rate of diffusion of the inert gas (dn/dt), correlating dn/dt with an overall mass transfer coefficient (K), correlating K with the mass transfer coefficient of the biofilm (ICB), and correlating kβ with the biofilm thickness. Also described is a membrane supported biofilm reactor (MSBR) of the type comprising a gas permeable membrane providing an interface between a lumen containing a gas phase, and a liquid phase, characterised in that the MSBR comprises means for flushing the lumen with an inert gas, means for closing and re-opening the lumen, and means for detecting intra-membrane pressure within the lumen. The means for detecting intra-membrane pressure is provided by a pressure transducer.

    摘要翻译： 一种评估膜支撑生物膜反应器（MSBR）中的生物膜厚度的方法，该生物膜反应器（MSBR）包括含有气相，液相和气体可渗透膜的腔，其提供气相和液相之间的界面，所述方法包括步骤 用惰性气体填充内腔，关闭内腔以在内腔中建立初始升高的压力，测量内腔内的压力变化率，并将压力变化率（dP / dt）与生物膜厚度相关联。 将dP / dt与生物膜厚度相关的步骤涉及将dP / dt与惰性气体扩散速率（dn / dt）相关联，将dn / dt与总传质系数（K）相关联，将K与质量传递相关联 生物膜（ICB）的系数，并将kβ与生物膜厚度相关联。 还描述了一种膜支持的生物膜反应器（MSBR），其包括提供在含有气相的内腔和液相之间的界面的气体可渗透膜，其特征在于，MSBR包括用惰性气体冲洗内腔的装置 用于关闭和重新打开内腔的装置，以及用于检测内腔内的膜内压力的装置。 用于检测膜内压力的装置由压力传感器提供。

    WATER TREATMENT APPARATUS
    7.
    发明申请
    WATER TREATMENT APPARATUS 审中-公开
    水处理设备

    公开(公告)号：WO2009062301A1

    公开(公告)日：2009-05-22

    申请号：PCT/CA2008/001998

    申请日：2008-11-12

    申请人： DAGUA INC. ,  LACASSE, Maurice

    发明人： LACASSE, Maurice

    IPC分类号： C02F1/20 ,  B01D19/00 ,  C02F1/78 ,  C02F9/02 ,  C02F9/04

    CPC分类号： C02F1/78 ,  B01D61/145 ,  B01D61/147 ,  B01D65/02 ,  B01D2311/04 ,  B01D2321/18 ,  C02F1/20 ,  C02F1/444 ,  C02F9/00 ,  C02F2201/782 ,  C02F2209/23 ,  C02F2301/046 ,  C02F2301/066 ,  C02F2303/14 ,  C02F2303/20 ,  C02F2303/22 ,  B01D2311/26 ,  B01D2311/2653

    摘要： An apparatus for an ozone-based treatment of polluted water is disclosed. The apparatus generally comprises three stages. The first stage is an ozone treatment stage wherein the polluted water is treated with ozone gas. The second stage is a degassing stage wherein excess undissolved gases are removed from the water whereby the water exiting the degassing stage is essentially saturated with gases. The last stage of the apparatus is a membrane filtration stage wherein the gas-saturated water generally undergoes micro- filtration or ultra-filtration. Microbubbles formed during this final stage generally prevent the accumulation of particles and pollutants on the surface of the membranes and/or inside the openings or pores thereof; thereby acting as a self-cleaning mechanism for the membrane filter.

    摘要翻译： 公开了一种用于臭氧处理污水的设备。 该装置通常包括三个阶段。 第一阶段是臭氧处理阶段，其中用臭氧气体处理污水。 第二阶段是脱气阶段，其中从水中除去过量的未溶解气体，由此离开脱气阶段的水基本上被气体饱和。 该装置的最后阶段是膜过滤阶段，其中气体饱和的水通常经历微过滤或超滤。 在该最终阶段期间形成的微泡通常防止颗粒和污染物在膜的表面和/或其开口或孔内的积聚; 从而作为膜过滤器的自清洁机构。

    AMMONIA REMOVAL APPARATUS AND METHOD
    8.
    发明申请
    AMMONIA REMOVAL APPARATUS AND METHOD 审中-公开
    AMMONIA移除装置和方法

    公开(公告)号：WO2009020517A1

    公开(公告)日：2009-02-12

    申请号：PCT/US2008/008812

    申请日：2008-07-18

    申请人： BASIN WATER - MPT, INC. ,  CRAFT, Frank, S., Sr.

    发明人： CRAFT, Frank, S., Sr.

    IPC分类号： B01D61/00

    CPC分类号： C02F1/42 ,  B01D2311/06 ,  C02F1/20 ,  C02F1/442 ,  C02F2001/425 ,  C02F2101/16 ,  C02F2103/10 ,  B01D2311/2626 ,  B01D2311/2623 ,  B01D2311/26

    摘要： An apparatus and method for removing ammonia from mining and other industrial wastewaters having a nanofiltration membrane separation system (10) to reject most divalent ions but pass most ammonium and other monovalent ions with the permeate (14) to a water softening system (20) with the effluent (21 ) to one or more strong acid cation NH 3 removal column(s) (30). Alkaline storage tank(s) (40, 50) provide for the regeneration of the NH 3 removal column(s) (30). A stripping tower (61 ) is provided for ammonia (NH 4 OH) removal.

    摘要翻译： 一种用于从具有纳滤膜分离系统（10）的采矿和其它工业废水中除去氨的装置和方法，用于排除大部分二价离子，但将大部分铵和其它一价离子与渗透物（14）一起通过水软化系统（20） 流出物（21）到一个或多个强酸性阳离子NH 3去除柱（30）。 碱性储罐（40,50）用于NH3去除塔（30）的再生。 提供用于去除氨（NH 4 OH）的汽提塔（61）。

    METHOD AND SYSTEM FOR MONITORING REVERSE OSMOSIS MEMBRANES
    9.
    发明申请
    METHOD AND SYSTEM FOR MONITORING REVERSE OSMOSIS MEMBRANES 审中-公开
    用于监测反转膜的方法和系统

    公开(公告)号：WO2007087578A3

    公开(公告)日：2007-10-18

    申请号：PCT/US2007060999

    申请日：2007-01-24

    申请人： UNIV CALIFORNIA ,  COHEN YORAM ,  UCHYMIAK MICHAL

    发明人： COHEN YORAM ,  UCHYMIAK MICHAL

    IPC分类号： B01D61/12 ,  B01D61/22 ,  B01D65/10

    CPC分类号： B01D61/12 ,  B01D61/025 ,  B01D65/08 ,  B01D65/10 ,  B01D2311/26 ,  B01D2321/00 ,  C02F1/441 ,  C02F2209/005 ,  Y02A20/131

    摘要： A monitoring system and a method for monitoring a reverse osmosis (RO) membrane in an RO unit is capable of detecting the formation of mineral salt crystals on the surface of the RO membrane. The monitoring system includes a reverse osmosis monitoring cell coupled to the RO unit so as to receive a sample stream taken from either the feed stream to, or the concentrate stream from, the RO unit. The cell has a visually-observable RO membrane that is visible to an imaging system that creates and collects images of the visually-observable RO membrane, and that conveys an image data signal to a data processing system that is operable to translate the image data signal into visual images for display, and to correlate the data in the image data signal with a scaling condition on the RO membrane in the RO unit.

    摘要翻译： 用于监测RO单元中的反渗透（RO）膜的监测系统和方法能够检测RO膜表面上矿物盐晶体的形成。 监测系统包括与RO单元相连的反渗透监测单元，以便接收来自RO单元的进料流或浓缩物流中的样品流。 细胞具有可视化的RO膜，其对于产生和收集可视观察的RO膜的图像的成像系统是可见的，并且将图像数据信号传送到数据处理系统，该数据处理系统可操作以将图像数据信号 转换为用于显示的视觉图像，并且将图像数据信号中的数据与RO单元中的RO膜上的缩放条件相关联。