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1. 发明专利

AU6230000A Water softening method and apparatus for use therewith 未知
公开(公告)号：AU6230000A
公开(公告)日：2001-02-05
申请号：AU6230000
申请日：2000-07-20
申请人： JUZER JANGBARWALA
发明人： JANGBARWALA JUZER
IPC分类号： B01J49/00 , C02F1/00 , C02F1/42

2. 发明授权

US08946111B2 Fibrous composite catalytic structure having at least three solid phases 有权
标题翻译：具有至少三个固相的纤维复合催化结构
公开(公告)号：US08946111B2
公开(公告)日：2015-02-03
申请号：US13680093
申请日：2012-11-18
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： B01J21/18 , B01J23/00 , B32B3/02 , B32B15/00 , B32B33/00 , B32B17/12 , B32B18/00 , B32B3/26 , B32B5/16 , B32B9/00 , B32B15/14 , B32B5/26 , B32B27/04 , B32B27/12 , D04H11/00 , D04H1/00 , D03D27/00 , D03D9/00 , D03D15/00 , D03D19/00 , D05C17/00 , B01J37/08 , B01J21/04 , B01J35/06 , B01J23/72 , B01J23/80 , C01B3/32 , B01J35/00 , B01J37/02 , B82Y30/00 , B01J37/34 , H01M8/06
CPC分类号： B01J37/08 , B01J21/04 , B01J21/18 , B01J21/185 , B01J23/72 , B01J23/80 , B01J35/0026 , B01J35/0033 , B01J35/06 , B01J37/0201 , B01J37/343 , B82Y30/00 , C01B3/326 , C01B2203/0233 , C01B2203/066 , C01B2203/1017 , C01B2203/1076 , C01B2203/1223 , H01M8/0631 , Y02P20/52 , Y10S977/742 , Y10T428/23921 , Y10T428/23986 , Y10T428/249928 , Y10T428/249929 , Y10T428/249953 , Y10T428/25 , Y10T428/2913 , Y10T428/2918 , Y10T428/2927 , Y10T428/294 , Y10T442/184 , Y10T442/186
摘要： Permeable composite fibrous catalytic sheets comprised of at least three distinct solid phases. A first solid phase is a 3-dimensional porous network of a non-conductive porous ceramic material. A second solid phase is an electrically conductive phase comprised of randomly oriented electrically conductive fibers. A third phase is comprised of catalytic particles dispersed on said 3-dimensional porous network, said conductive fibers, or both. A fourth phase can be present, which fourth phase is comprised one or more conductive species or one or more non conductive species embedded in said first solid phase.
摘要翻译：由至少三个不同固相组成的可渗透复合纤维状催化片。第一固相是非导电多孔陶瓷材料的三维多孔网络。第二固相是由随机取向的导电纤维组成的导电相。第三相包括分散在所述三维多孔网络，所述导电纤维或两者上的催化颗粒。可以存在第四相，该第四相包含一种或多种导电物质或嵌入所述第一固相中的一种或多种非导电物质。

3. 发明授权

US07470413B2 Fluorine removal by ion exchange 失效
标题翻译：通过离子交换除氟
公开(公告)号：US07470413B2
公开(公告)日：2008-12-30
申请号：US10759718
申请日：2004-01-16
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： B01D53/68 , C02F1/42 , B01J49/00
CPC分类号： B01D53/68 , B01D53/73 , B01D53/96 , B01D2257/2027 , B01J41/05 , B01J41/07 , B01J47/016 , B01J49/50 , Y02C20/30
摘要： A method for removing fluorine gas from a selected environment comprises contacting the fluorine gas with water to generate a solution of hydrofluoric acid and contacting the solution of hydrofluoric acid with an ion exchange resin having an active state operative to exchange selected ions therein for fluoride ions in the solution. The apparatus (200) may include a dual resin setup (222, 223) such that one of the ion-exchange resin can be in the service cycle while the other of the ion-exchange resins undergoes the regeneration and rinse/refill cycles.
摘要翻译：从所选择的环境中除去氟气的方法包括使氟气与水接触以产生氢氟酸溶液，并使氢氟酸溶液与具有活性状态的离子交换树脂接触，以在其中交换选定的离子用于氟离子解决方案。装置（200）可以包括双重树脂装置（222,223），使得一个离子交换树脂可以处于使用循环中，而另一个离子交换树脂经历再生和冲洗/再填充循环。

4. 发明专利

NZ539973A Application of conductive absorbents, activated carbon granules and carbon fibers as substrates in catalysis 未知
公开(公告)号：NZ539973A
公开(公告)日：2008-03-28
申请号：NZ53997303
申请日：2003-11-19
申请人： JUZER JANGBARWALA
发明人： JANGBARWALA JUZER
IPC分类号： B01D53/88 , B01J8/02 , B01J19/08 , B01J21/18 , B01J23/00 , B01J23/16 , B01J23/40 , B01J23/70 , B01J23/80 , B01J31/08 , B01J35/06 , B01J35/08 , C25B3/00 , C25D17/00
摘要： Disclosed is a method for conducting a chemical reaction in the presence of a catalyst, wherein the method comprises: providing said catalyst on a support of electrically conductive carbonaceous material comprised of carbon fibers and carbon nanotubes; and supplying an electric current to said support such that said support passes said electric current to said catalyst, wherein electrical resistively heats said catalyst to a temperature effective to activate the catalyst.

5. 发明授权

US08598240B2 Fischer-tropsch process using fibrous composite catalytic structures having at least three solid phases 失效
标题翻译：使用具有至少三个固相的纤维复合催化结构的费 - 托法
公开(公告)号：US08598240B2
公开(公告)日：2013-12-03
申请号：US13680416
申请日：2012-11-19
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： C07C27/00
CPC分类号： C07C1/048 , B01J21/18 , B01J23/80 , B01J29/85 , B01J35/0033 , B01J35/023 , B01J35/06 , B01J37/0201 , B01J37/343 , C01B3/326 , C01B2203/0233 , C01B2203/066 , C01B2203/1017 , C01B2203/1076 , C01B2203/1223 , C07C1/0425 , H01M8/0631 , Y02P20/52
摘要： A Fischer-Tropsch process for converting a syngas to hydrocarbon products in the presence of a permeable composite fibrous catalytic sheet comprised of at least three distinct solid phases. A first solid phase is a 3-dimensional porous network of a non-conductive porous ceramic material. A second solid phase is an electrically conductive phase comprised of randomly oriented electrically conductive fibers. A third phase is comprised of catalytic particles dispersed on said 3-dimensional porous network, said conductive fibers, or both. A fourth phase can be present, which fourth phase is comprised one or more conductive species or one or more non-conductive species embedded in said first solid phase.
摘要翻译：在由至少三个不同固相组成的可渗透复合纤维催化片存在下，将合成气转化为烃产物的费 - 托法。第一固相是非导电多孔陶瓷材料的三维多孔网络。第二固相是由随机取向的导电纤维组成的导电相。第三相包括分散在所述三维多孔网络，所述导电纤维或两者上的催化颗粒。可以存在第四相，该第四相包含一种或多种导电种类或嵌入所述第一固相中的一种或多种非导电物质。

6. 发明申请

US20130092877A1 Methane Steam Reforming Using Fibrous Composite Catalytic Structures Having at Least Three Solid Phases 失效
标题翻译：使用具有至少三个固相的纤维复合催化结构的甲烷蒸汽重整
公开(公告)号：US20130092877A1
公开(公告)日：2013-04-18
申请号：US13680510
申请日：2012-11-19
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： C01B3/40
CPC分类号： C01B3/40 , B01J21/04 , B01J21/18 , B01J21/185 , B01J23/24 , B01J23/38 , B01J23/74 , B01J23/80 , B01J27/1856 , B01J35/0006 , B01J35/0033 , B01J35/023 , B01J35/06 , B01J35/065 , B01J35/1014 , B01J35/1019 , B01J35/1028 , B01J37/0201 , B01J37/343 , B82Y30/00 , C01B3/326 , C01B2203/0233 , C01B2203/0283 , C01B2203/0405 , C01B2203/043 , C01B2203/0445 , C01B2203/066 , C01B2203/1017 , C01B2203/1041 , C01B2203/1058 , C01B2203/1064 , C01B2203/1076 , C01B2203/1223 , C01B2203/142 , H01M8/0631 , Y02P20/52 , Y10S977/734 , Y10S977/742
摘要： A methane steam reforming process for converting a syngas in the presence of permeable composite fibrous catalytic sheets comprised of at least three distinct solid phases. A first solid phase is a 3-dimensional porous network of a non-conductive porous ceramic material. A second solid phase is an electrically conductive phase comprised of randomly oriented electrically conductive fibers. A third phase is comprised of methane steam reforming catalytic particles dispersed on said 3-dimensional porous network, said conductive fibers, or both. A fourth phase can be present, which fourth phase is comprised one or more conductive species or one or more non-conductive species embedded in said first solid phase.
摘要翻译：甲烷蒸汽重整方法，用于在由至少三个不同的固相组成的可渗透的复合纤维催化片存在下转化合成气。第一固相是非导电多孔陶瓷材料的三维多孔网络。第二固相是由随机取向的导电纤维组成的导电相。第三相包括分散在所述三维多孔网络，所述导电纤维或两者上的甲烷蒸汽重整催化颗粒。可以存在第四相，该第四相包含一种或多种导电种类或嵌入所述第一固相中的一种或多种非导电物质。

7. 发明授权

US08168068B2 Treatment of contaminated water streams from coal-bed-methane production 失效
标题翻译：处理煤层气生产污染水流
公开(公告)号：US08168068B2
公开(公告)日：2012-05-01
申请号：US12460956
申请日：2009-07-27
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： B01J49/00
CPC分类号： C02F1/42 , B01J39/07 , B01J49/06 , B01J49/53 , C02F2001/425 , C02F2103/10 , C02F2303/16
摘要： The present invention is a method for treating contaminated water streams resulting from the production of coal-bed-methane. The method of treating contaminated water streams typically includes the steps of: providing a reaction vessel that contains a bed of weak acid cation ion exchange resin beads; introducing the contaminated water stream to the reaction vessel; allowing for the exchange of hydrogen ions for sodium ions; removing the ion exchanged treated water from the reaction vessel; stopping the stream of contaminated water; and regenerating the weak cation exchange resin.
摘要翻译：本发明是一种处理由煤层气生成产生的污水的方法。处理受污染水流的方法通常包括以下步骤：提供含有弱酸性阳离子离子交换树脂珠床的反应容器; 将污染的水流引入反应容器中; 允许氢离子交换钠离子; 从反应容器中除去离子交换的处理过的水; 停止受污染的水流; 并再生弱阳离子交换树脂。

8. 发明申请

US20060254919A1 Electrophoretic cross-flow filtration and electrodeionization method for treating effluent waste and apparatus for use therewith 审中-公开
标题翻译：用于处理废水的电泳交叉流过滤和电去离子法及其使用的设备
公开(公告)号：US20060254919A1
公开(公告)日：2006-11-16
申请号：US11353906
申请日：2006-02-14
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： C02F1/469 , C02F1/461
CPC分类号： B01J47/08 , B01D57/02 , B01D61/425 , B01D61/48 , B01D65/08 , B01D2321/2025 , C02F1/4695 , C02F1/4696 , C02F2101/20 , C02F2103/346
摘要： The present invention provides a method and apparatus for purifying effluent wastewater utilizing electrophoretic cross-flow filtration and electrode ionization. The method first comprises filtering the water in a cross-flow direction with a filter membrane in the presence of an electric field that is operative to drive suspended particles away from a surface of the filter membrane. The permeate containing dissolved solids is next passed through a mixture of at least one cation-exchange resin and at least one anion-exchange resin disposed between a cation-selective membrane and an anion-selective membrane in the presence of an electric field. The electric field drives cations in the permeate through the cation-selective membrane, and drives anions in the permeate through the anion-selective membrane, thereby to form deionized water. The apparatus includes cell modules adapted to be used in plate-and-frame or radial flow configurations.
摘要翻译：本发明提供一种利用电泳交叉流过滤和电极电离来净化废水的废水的方法和装置。该方法首先包括在存在电场的情况下用过滤膜在交叉流动方向上过滤水，其可操作地驱动悬浮颗粒远离过滤膜的表面。含有溶解的固体的渗透物接着在存在电场的情况下通过至少一种阳离子交换树脂和设置在阳离子选择性膜和阴离子选择性膜之间的至少一种阴离子交换树脂的混合物。电场通过阳离子选择性膜驱动渗透物中的阳离子，并且通过阴离子选择性膜驱使渗透物中的阴离子，从而形成去离子水。该装置包括适用于平板和框架或径向流动构造的单元模块。

9. 发明授权

US06998054B2 Selective fluoride and ammonia removal by chromatographic separation of wastewater 失效
公开(公告)号：US06998054B2
公开(公告)日：2006-02-14
申请号：US10749954
申请日：2003-12-31
申请人： Juzer Jangbarwala , Gerald Albert Krulik
发明人： Juzer Jangbarwala , Gerald Albert Krulik
IPC分类号： B01D15/08
CPC分类号： B01D15/363 , B01D15/362 , B01J39/05 , B01J49/08 , C02F2001/422 , C02F2001/425 , B01J41/05 , B01J41/07
摘要： A process for fluoride removal from wastewater streams produced during industrial operation for further industrial use or to comply with environmental regulations. The process segregates the removal of fluoride and fluorosilicate ions, from the totality of ions in the waste water stream, thus improving treatment efficiency and reducing costs. Ion-exchange chromatography is used to remove the fluoride and fluorosilicate ions by passing the wastewater stream through one or more columns that contain a charged resin which selectively binds cations/anions in the stream. The fluoride ions are washed from the column and then collected for removal or use in other processes.

10. 发明授权

US06835295B1 Electrowinning cell incorporating metal ion filtration apparatus 有权
标题翻译：电泳细胞结合金属离子过滤装置
公开(公告)号：US06835295B1
公开(公告)日：2004-12-28
申请号：US10009710
申请日：2001-11-28
申请人： Juzer Jangbarwala
发明人： Juzer Jangbarwala
IPC分类号： C25B1500
CPC分类号： C25C7/06 , C25C7/00
摘要： An apparatus and method for electrowinning metal from ionic solutions is provided wherein ionic solution is subject to nanofiltration. An electrowinning cell (10) includes a reservoir (12) adapted to receive an ionic solution (14). During operation, metal ions in solution (14) electroplate onto cathode (18). Nanofilter (20) is in fluid communication with the reservoir and receives solution (14) from a location (22) proximate to the cathode (18). Retentate (52) is formed as a first portion (26) of the solution (14) which passes through the membrane (21) of the filter (20). Permeate (54) is formed as a second portion (28) of the solution (14) which passes through the membrane (21) of the filter (20) to a second region (29) on the opposite side of membrane (21) from the first region (27). Permeate (54) has a second concentration of metal ions lower than the first concentration in first portion (26). Retentate (52) is returned to the reservoir (12) to intermix with solution (14).
摘要翻译：提供了一种从离子溶液中电解金属的装置和方法，其中离子溶液进行纳米过滤。电解提取电池（10）包括适于接收离子溶液（14）的储存器（12）。在操作过程中，溶液（14）中的金属离子电镀到阴极（18）上。纳滤器（20）与储存器流体连通并且从靠近阴极（18）的位置（22）接收溶液（14）。半导体（52）形成为通过过滤器（20）的膜（21）的溶液（14）的第一部分（26）。渗透物（54）形成为溶液（14）的第二部分（28），其通过过滤器（20）的膜（21）到膜（21）的相对侧上的第二区域（29）第一个地区（27）。渗透物（54）在第一部分（26）中具有低于第一浓度的第二浓度的金属离子。滞留物（52）返回储存器（12）以与溶液（14）混合。

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