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1. 发明申请

US20070215474A1 Electrodialysis System and Process 有权
标题翻译：电渗析系统和工艺
公开(公告)号：US20070215474A1
公开(公告)日：2007-09-20
申请号：US10577120
申请日：2004-10-27
申请人： Bruce Batchelder , Li Zhang , William Carson
发明人： Bruce Batchelder , Li Zhang , William Carson
IPC分类号： B01D61/44 , B01D61/46 , B01D61/48 , B01D61/54
CPC分类号： B01D61/48 , B01D61/422 , B01D61/44 , B01D61/46 , B01D61/54 , B01D61/58 , B01D65/02 , B01D65/027 , B01D2311/243 , B01D2317/04 , B01D2321/16 , B01D2321/162 , C02F1/469 , C02F1/4693 , C02F1/4695
摘要： A treatment system and method for continuous deionization of a biologically derived feed stream includes a plurality of electrodialysis units (3, 9, 10, 11, 12, 13) arranged in stages along a treatment line, and stages are controlled such that the feed stream attains a certain quality before entering the next stage. The feed and concentrate streams move in generally opposite sense along the line, matching fluid characteristics of dilute and concentrate cells. The treatment line has two or more stages. Systems may have phased staging operations, and cell constructions may adapt the electrodialysis units for enhanced processing of difficult process fluids. A controller sets operating potentials in different electrical stages, and simple control parameters optimize ion removal and current efficiency without polarization of the fluid. The invention also includes phased staging of reversal operation, and cell constructions or fillings that adapt the treatment cells for enhanced processing.
摘要翻译：用于生物衍生的进料流的连续去离子的处理系统和方法包括沿着处理管线分阶段布置的多个电渗析单元（3,9,10,11,12,13），并且控制阶段使得进料流在进入下一阶段之前达到一定的质量。进料和浓缩物流沿着整条相反的方向移动，匹配稀释和浓缩细胞的流体特性。治疗线有两个或更多个阶段。系统可以具有阶段性分段操作，并且细胞结构可以适应电渗析单元以增强难处理流体的处理。控制器在不同的电气阶段设置工作电位，简单的控制参数可优化离子去除和电流效率，而无需流体的极化。本发明还包括反转操作的阶段分阶段，以及适应处理单元以增强处理的单元结构或填充物。

2. 发明申请

US20060169581A1 Spiral electrodeionization device with flow distribution profiling 有权
标题翻译：具有流量分布曲线的螺旋电去离子装置
公开(公告)号：US20060169581A1
公开(公告)日：2006-08-03
申请号：US11292319
申请日：2005-12-01
申请人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
发明人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
IPC分类号： C25B9/08
CPC分类号： B01D61/46 , B01D61/48 , B01D61/52 , B01D63/10 , B01J47/08 , C02F1/4695 , C02F2201/003
摘要： EDI apparatus for demineralizing a liquid flow is assembled in a housing having a cylindrical shape, and includes two metal electrodes, and one or more leafs, each leaf comprising a pair of selectively ion-permeable membranes arranged parallel to each other and spaced apart by spacing elements that allow liquid to flow in the interstitial space between membranes, thus forming an arrangement of dilute and concentrate cells in a desired flow configuration. Spacing elements between membranes, as well as between leaves, can be formed of inert polymer material, ion exchange beads, ion exchange fibers, a combination of two or more these elements, or a porous media incorporating one or more of such elements as an intrinsic part. An inner or central electrode and an outer or perimeter electrode establish a generally uniform and radially-oriented electrical or ionic current between the inner and the outer electrodes, across the helical flow spaces defined by the membrane/spacer windings. One or both electrodes may include a pocket, and the adjacent flow cells lie parallel to the electrode and free of shadowing and field inhomogeneity around a full circumference of the electrode. Flow paths within the helical cells are defined by barrier seals, which may form a path-lengthening maze, while unfilled cell regions may disperse or collect flow within a cell and define pressure gradients promote directional flows. Impermeable barriers between membranes further prevent the feed and concentrate flows from mixing. In various embodiments, seals along or between portions of the flow path may define a multi-stage device, may define separate feed and/or concentrate flows for different stages, and/or may direct the feed and concentrate flows along preferred directions which may be co-current, counter-current or cross-current with respect to each other within the apparatus.
摘要翻译：用于使液体流动脱矿质的EDI装置组装在具有圆柱形形状的壳体中，并且包括两个金属电极和一个或多个叶片，每个叶片包括一对彼此平行布置的间隔开的间隔开的间隔开的选择性离子渗透膜允许液体在膜之间的间隙空间中流动的元件，从而在期望的流动构型中形成稀释和浓缩细胞的排列。膜之间以及叶之间的间隔元件可以由惰性聚合物材料，离子交换珠，离子交换纤维，两种或更多种这些元素的组合形成，或多种介质结合一种或多种这样的元素，如内在的部分。内部或中心电极和外部或周边电极在内部和外部电极之间跨越由膜/间隔件绕组限定的螺旋流动空间建立大致均匀且径向取向的电或离子电流。一个或两个电极可以包括袋，并且相邻的流动池平行于电极并且在电极的整个周围没有阴影和场不均匀性。螺旋细胞内的流动路径由阻挡密封件限定，其可以形成路径延长迷宫，而未填充的细胞区域可以在细胞内分散或收集流动并且限定压力梯度促进定向流动。膜之间的不渗透屏障进一步防止了进料和浓缩物的流动。在各种实施例中，沿着流动路径的部分或之间的密封件可以限定多级装置，可以为不同的级限定单独的进料和/或浓缩物流，和/或可以将进料和浓缩物流沿着优选的方向引导，在设备内相互相互并流，逆流或交叉电流。

3. 发明申请

US20060169580A1 Spiral electrodeionization device with segregated ionic flows 有权
标题翻译：具有分离离子流的螺旋电去离子装置
公开(公告)号：US20060169580A1
公开(公告)日：2006-08-03
申请号：US11291526
申请日：2005-12-01
申请人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
发明人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
IPC分类号： C25B9/08
CPC分类号： C02F1/4695 , B01D61/46 , B01D61/48 , B01D61/52 , B01D63/10 , B01J47/08 , C02F2001/46152 , C02F2201/003 , C02F2201/4611
摘要： EDI apparatus for demineralizing a liquid flow is assembled in a housing having a cylindrical shape, and includes two metal electrodes, and one or more leafs, each leaf comprising a pair of selectively ion-permeable membranes arranged parallel to each other and spaced apart by spacing elements that allow liquid to flow in the interstitial space between membranes, thus forming an arrangement of dilute and concentrate cells in a desired flow configuration. Spacing elements between membranes, as well as between leaves, can be formed of inert polymer material, ion exchange beads, ion exchange fibers, a combination of two or more these elements, or a porous media incorporating one or more of such elements as an intrinsic part. An inner or central electrode and an outer or perimeter electrode establish a generally uniform and radially-oriented electrical or ionic current between the inner and the outer electrodes, across the helical flow spaces defined by the membrane/spacer windings. One or both electrodes may include a pocket, and the adjacent flow cells lie parallel to the electrode and free of shadowing and field inhomogeneity around a full circumference of the electrode. Flow paths within the helical cells are defined by barrier seals, which may form a path-lengthening maze, while unfilled cell regions may disperse or collect flow within a cell and define pressure gradients promote directional flows. Impermeable barriers between membranes further prevent the feed and concentrate flows from mixing. In various embodiments, seals along or between portions of the flow path may define a multi-stage device, may define separate feed and/or concentrate flows for different stages, and/or may direct the feed and concentrate flows along preferred directions which may be co-current, counter-current or cross-current with respect to each other within the apparatus.
摘要翻译：用于使液体流动脱矿质的EDI装置组装在具有圆柱形形状的壳体中，并且包括两个金属电极和一个或多个叶片，每个叶片包括一对彼此平行布置的间隔开的间隔开的间隔开的选择性离子渗透膜允许液体在膜之间的间隙空间中流动的元件，从而在期望的流动构型中形成稀释和浓缩细胞的排列。膜之间以及叶之间的间隔元件可以由惰性聚合物材料，离子交换珠，离子交换纤维，两种或更多种这些元素的组合形成，或多种介质结合一种或多种这样的元素，如内在的部分。内部或中心电极和外部或周边电极在内部和外部电极之间跨越由膜/间隔件绕组限定的螺旋流动空间建立大致均匀且径向取向的电或离子电流。一个或两个电极可以包括袋，并且相邻的流动池平行于电极并且在电极的整个周围没有阴影和场不均匀性。螺旋细胞内的流动路径由阻挡密封件限定，其可以形成路径延长迷宫，而未填充的细胞区域可以在细胞内分散或收集流动并且限定压力梯度促进定向流动。膜之间的不渗透屏障进一步防止了进料和浓缩物的流动。在各种实施例中，沿着流动路径的部分或之间的密封件可以限定多级装置，可以为不同的级限定单独的进料和/或浓缩物流，和/或可以将进料和浓缩物流沿着优选的方向引导，在设备内相互相互并流，逆流或交叉电流。

4. 发明申请

US20060163056A1 Spiral electrodeionization device with uniform operating characteristics 审中-公开
标题翻译：具有均匀运行特性的螺旋电去离子装置
公开(公告)号：US20060163056A1
公开(公告)日：2006-07-27
申请号：US11291528
申请日：2005-12-01
申请人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
发明人： Vladimir Grebenyuk , Oleg Grebenyuk , Keith Sims , William Carson , Russell MacDonald , Li Zhang
IPC分类号： C25C7/02
CPC分类号： C02F1/4695 , B01D61/46 , B01D61/48 , B01D61/52 , B01D63/10 , B01J47/08 , C02F2001/46152 , C02F2201/003 , C02F2201/4611
摘要： EDI apparatus for demineralizing a liquid flow is assembled in a housing having a cylindrical shape, and includes two metal electrodes, and one or more leafs, each leaf comprising a pair of selectively ion-permeable membranes arranged parallel to each other and spaced apart by spacing elements that allow liquid to flow in the interstitial space between membranes, thus forming an arrangement of dilute and concentrate cells in a desired flow configuration. Spacing elements between membranes, as well as between leaves, can be formed of inert polymer material, ion exchange beads, ion exchange fibers, a combination of two or more these elements, or a porous media incorporating one or more of such elements as an intrinsic part. An inner or central electrode and an outer or perimeter electrode establish a generally uniform and radially-oriented electrical or ionic current between the inner and the outer electrodes, across the helical flow spaces defined by the membrane/spacer windings. One or both electrodes may include a pocket, and the adjacent flow cells lie parallel to the electrode and free of shadowing and field inhomogeneity around a full circumference of the electrode. Flow paths within the helical cells are defined by barrier seals, which may form a path-lengthening maze, while unfilled cell regions may disperse or collect flow within a cell and define pressure gradients promote directional flows. Impermeable barriers between membranes further prevent the feed and concentrate flows from mixing. In various embodiments, seals along or between portions of the flow path may define a multi-stage device, may define separate feed and/or concentrate flows for different stages, and/or may direct the feed and concentrate flows along preferred directions which may be co-current, counter-current or cross-current with respect to each other within the apparatus.
摘要翻译：用于使液体流动脱矿质的EDI装置组装在具有圆柱形形状的壳体中，并且包括两个金属电极和一个或多个叶片，每个叶片包括一对彼此平行布置的间隔开的间隔开的间隔开的选择性离子渗透膜允许液体在膜之间的间隙空间中流动的元件，从而在期望的流动构型中形成稀释和浓缩细胞的排列。膜之间以及叶之间的间隔元件可以由惰性聚合物材料，离子交换珠，离子交换纤维，两种或更多种这些元素的组合形成，或多种介质结合一种或多种这样的元素，如内在的部分。内部或中心电极和外部或周边电极在内部和外部电极之间跨越由膜/间隔件绕组限定的螺旋流动空间建立大致均匀且径向取向的电或离子电流。一个或两个电极可以包括袋，并且相邻的流动池平行于电极并且在电极的整个周围没有阴影和场不均匀性。螺旋细胞内的流动路径由阻挡密封件限定，其可以形成路径延长迷宫，而未填充的细胞区域可以在细胞内分散或收集流动并且限定压力梯度促进定向流动。膜之间的不渗透屏障进一步防止了进料和浓缩物的流动。在各种实施例中，沿着流动路径的部分或之间的密封件可以限定多级装置，可以为不同的级限定单独的进料和/或浓缩物流，和/或可以将进料和浓缩物流沿着优选的方向引导，在设备内相互相互并流，逆流或交叉电流。

5. 发明申请

US20180093049A1 SYRINGE GUIDE AND METHOD FOR ITS USE 审中-公开
公开(公告)号：US20180093049A1
公开(公告)日：2018-04-05
申请号：US15282316
申请日：2016-09-30
申请人： William Carson
发明人： William Carson
IPC分类号： A61M5/46 , A61M5/31
CPC分类号： A61M5/46 , A61M5/31
摘要： A syringe guide includes: a syringe receiver including a receptacle configured to retain a syringe therein; a depth guide defining a reference surface; and a depth adjustment mechanism interconnecting the syringe receiver and the depth guide, and operable to change a distance between the receptacle and the reference surface.

6. 发明申请

US20050120345A1 Methods and systems for instantly closing browser windows 审中-公开
标题翻译：立即关闭浏览器窗口的方法和系统
公开(公告)号：US20050120345A1
公开(公告)日：2005-06-02
申请号：US10804577
申请日：2004-03-19
申请人： William Carson
发明人： William Carson
IPC分类号： G06F3/00 , G06F9/445
CPC分类号： G06F9/451
摘要： Software that causes browser windows and other windows to instantly disappear from a computer screen upon activation of a function activator. Preferably, when a user activates the function activator, the software also causes any open browser applications to shut down as well. The function activator may comprise an icon displayed on the computer screen or a physical switch coupled to the software. Moreover, the software may be incorporated into an Internet Service Provider's browser software or be installed separately from the installation of the browser on the individual user's computer.
摘要翻译：导致浏览器窗口和其他窗口在激活函数激活器时立即从计算机屏幕消失的软件。优选地，当用户激活功能激活器时，软件也使得任何打开的浏览器应用也被关闭。功能激活器可以包括显示在计算机屏幕上的图标或耦合到软件的物理开关。此外，该软件可以被合并到因特网服务提供商的浏览器软件中，或者与个人用户计算机上的浏览器的安装分开安装。

7. 发明授权

US4726918A Packing element 失效
标题翻译：包装要素
公开(公告)号：US4726918A
公开(公告)日：1988-02-23
申请号：US902969
申请日：1986-09-02
申请人： William Carson
发明人： William Carson
IPC分类号： B01J19/30 , F28F25/08 , B01F3/04
CPC分类号： F28F25/08 , B01J19/30 , B01J2219/3023 , B01J2219/30238 , B01J2219/30296 , B01J2219/30408 , B01J2219/30416 , B01J2219/30433 , B01J2219/30466 , Y10S261/72
摘要： This invention is a packing for use in a packed tower. The packing has four axes and six webs and is symmetrical around each axes. The packing is of a geometrical configuration that with one of the axes pointing downwardly and the other three axes pointing upwardly and above the downwardly pointing axes the fluid can flow towards the center of the packing into an opening at its center. In the configuration with the three axes pointing downwardly and the one axis pointing upwardly the fluid is directed away from the center of the packing and flows off of the webs. With this geometrical configuration the flow of the fluid is evenly distributed throughout the packed bed.
摘要翻译：本发明是用于填充塔的包装。包装有四个轴和六个腹板，围绕每个轴对称。包装是几何构型，其中一个轴指向下方，另外三个轴指向向上和向上指向的轴上方，流体可以朝着包装的中心流动到其中心的开口中。在三个轴向下指向并且一个轴向上指向的构造中，流体被引导离开填料的中心并从腹板流出。利用这种几何构型，流体的流动均匀地分布在整个填充床中。

8. 发明申请

US20070138008A1 Spacer For Filled Cell Electrodialysis 有权
标题翻译：填充细胞电渗析的间隔物
公开(公告)号：US20070138008A1
公开(公告)日：2007-06-21
申请号：US10495394
申请日：2002-11-16
申请人： William Carson
发明人： William Carson
IPC分类号： C25B13/00
CPC分类号： B01D69/06 , B01D61/48 , B01D61/50 , B01D2313/08 , B01D2325/06 , B01J47/08 , C02F1/4604 , C02F1/469 , C02F2201/46115
摘要： A spacer element (1) is disclosed having an integral screen for use in filled cell electrodialysis. The spacer (1) has a continuous portion (2) impermeable to flow and a screen (3) which spans a centrally-located flow treatment region that contains active treatment material, such as ion exchange beads. The screen (3) may perform a structural function, allowing operation at elevated pressure, and may also define a minimum gap between adjacent membranes and enhance mixing along the flow path and at cell boundaries. The spacer element (1) may be configured to enhance hydraulic filling of the cells, and cell architecture is readily implemented in a wide range of useful flow path geometries utilizing the screen spacer element (1).
摘要翻译：公开了一种间隔元件（1），其具有用于填充电池电渗析的整体屏幕。隔离物（1）具有不可渗透的连续部分（2）和跨过包含活性处理材料（例如离子交换珠）的位于中心的流动处理区域的筛网（3）。屏幕（3）可以执行结构功能，允许在升高的压力下操作，并且还可以限定相邻膜之间的最小间隙并且增强沿着流动路径和在单元边界处的混合。间隔元件（1）可以被配置为增强电池的液压填充，并且使用屏幕间隔元件（1），在宽范围的有用流路几何形状中容易地实现电池结构。

9. 发明申请

US20050230857A1 Heat recovery using fluidized spray tower 有权
标题翻译：使用流化喷雾塔进行热回收
公开(公告)号：US20050230857A1
公开(公告)日：2005-10-20
申请号：US11104981
申请日：2005-04-12
申请人： William Carson
发明人： William Carson
IPC分类号： F02G5/02 , F23N5/24 , F28C3/06 , F28C3/08 , C10K1/00
CPC分类号： F23J15/06 , F23N5/242 , Y02E20/363 , Y10S261/09
摘要： A fluidized spray vessel. A vessel design is provided for recovering heat from gaseous heat streams. The vessel utilizes a semi-fluidized bed for obtaining desirable liquid/vapor contact times. A spray section is provided in which liquid is sprayed through nozzles designed to provide a mean droplet size having a terminal velocity of from about sixty percent to about ninety five percent of the superficial upward gas velocity. These spray tower design criteria enhance spray tower performance, and thus enables more efficient heat recovery to be practiced, particularly in systems where relatively low grade heat sources are encountered.
摘要翻译：流化喷雾容器。提供了用于从气体热流回收热量的容器设计。容器利用半流化床获得所需的液体/蒸汽接触时间。提供喷射部分，其中通过喷嘴喷射液体，喷嘴被设计成提供平均液滴尺寸，其终点速度为表面向上气体速度的约百分之六十至百分之九十五。这些喷射塔设计标准提高了喷雾塔的性能，从而能够实现更有效的热回收，特别是在遇到相对低等级的热源的系统中。

10. 发明申请

US20070051684A1 Sparse media edi apparatus and method 审中-公开
公开(公告)号：US20070051684A1
公开(公告)日：2007-03-08
申请号：US10527766
申请日：2003-09-12
申请人： Vladimir Grebenyuk , William Carson , Oleg Grebenyuk , Keith Sims , Russell MacDonald
发明人： Vladimir Grebenyuk , William Carson , Oleg Grebenyuk , Keith Sims , Russell MacDonald
IPC分类号： C02F1/42 , B01D71/82
CPC分类号： C02F1/4695 , B01D61/48 , B01D2313/30 , B01J47/08 , C02F2201/46115 , C02F2303/16
摘要： An electrodeionization, (EDI) apparatus has flow cells with a sparse distribution of ion exchange (IX) material or beads. The beads extend between membranes defining opposed walls of the cell to separate and support the membranes, and form a layer substantially free of bead-to-bead dead-end reverse junctions. The beads enhance capture of ions from surrounding fluid in dilute cells, and do not throw salt when operating current is increased. In concentrating cells, the sparse bead filling provides a stable low impedance bridge to enhanced power utilization in the stack. A monotype sparse filling may be used in concentrate cells, while mixed, layered, striped, graded or other beads may be employed in dilute cells. Ion conduction paths are no more than a few grains long and the lower packing density permits effective fluid flow. A flow cell thickness may be below one millimeter, and the beads may be discretely spaced, form a mixed or patterned monolayer, or form an ordered bilayer, and a mesh having a lattice spacing comparable to or of the same order of magnitude as resin grain size, may provide a distributed open support that assures a stable distribution of the sparse filling, and over time maintains the initial balance of uniform conductivity and good through-flow. The cells or low thickness and this resin layers relax stack size and power supply constraints, while providing treatment efficiencies and process stability. Reduced ion migration distances enhance the ion removal rate without reducing the product flow rate. The sparse resin bed may be layered, graded along the length of the path, striped or otherwise patterned. Inter-grain ion hopping is reduced or eliminated, thus avoiding the occurrence of salt-throwing which occurs at reverse bead junctions of prior art constructions. Conductivity of concentrate cells is increased, permitting more compact device construction, allowing increases in stack cell number, and providing more efficient electrical operation without ion additions. Finally, ion storage within beads is greatly reduces, eliminating the potential for contamination during reversal operation. Various methods of forming sparse beds and assembling the stacks are disclosed.

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