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1. 发明申请

US20100228025A1 STRUCTURED ORGANIC FILMS HAVING AN ADDED FUNCTIONALITY 有权
标题翻译：具有添加功能的结构有机膜
公开(公告)号：US20100228025A1
公开(公告)日：2010-09-09
申请号：US12716449
申请日：2010-03-03
申请人： Adrien Pierre COTE , Matthew A. HEUFT
发明人： Adrien Pierre COTE , Matthew A. HEUFT
IPC分类号： C07D265/00 , C07C211/00 , C07C43/00 , C07D209/96 , C07D409/02 , B05D3/02
CPC分类号： G03G5/0618 , B82Y10/00 , B82Y30/00 , C09B3/00 , C09B5/62 , C09B23/12 , C09B23/148 , C09B26/02 , C09B57/008 , G03G5/0592 , G03G5/0596 , G03G5/14791 , G03G5/14795 , G03G15/75 , G03G2215/00957 , H01L51/0002 , H01L51/0003 , H01L51/0007 , H01L51/0014 , H01L51/002 , H01L51/0026 , H01L51/003 , H01L51/0034 , H01L51/0045 , H01L51/005 , H01L51/0077 , H01L51/0093 , H01L51/052 , H01L51/0558 , H01L51/0595 , H01L51/5012 , H01L51/502 , H01L51/5024 , H01L51/5203 , Y10T428/26 , Y10T428/261 , Y10T428/31504
摘要： A structured organic film with an added functionality comprising a plurality of segments and a plurality of linkers arranged as a covalent organic framework, wherein the structured organic film may be a multi-segment thick structured organic film.
摘要翻译：具有附加功能的结构化有机膜包括多个片段和布置成共价有机骨架的多个接头，其中所述结构化有机膜可以是多段厚结构化有机膜。

2. 发明申请

US20070114174A1 Apparatus and Method for Treating FGD Blowdown or Similar Liquids 有权
标题翻译：用于处理烟气脱硫或类似液体的设备和方法
公开(公告)号：US20070114174A1
公开(公告)日：2007-05-24
申请号：US11609089
申请日：2006-12-11
申请人： Jeffrey Peeters , William Bonkoski , Pierre Cote , Hidayat Husain
发明人： Jeffrey Peeters , William Bonkoski , Pierre Cote , Hidayat Husain
IPC分类号： C02F3/30
CPC分类号： C02F3/302 , C02F3/006 , C02F3/06 , C02F2003/003 , C02F2101/101 , C02F2101/106 , C02F2101/20 , C02F2103/18 , C02F2209/04 , Y02E50/343 , Y02W10/15 , Y10S210/903 , Y10S210/912 , Y10S210/914
摘要： A process has steps of one or more of aerobic treatment to remove COD and nitrify a waste stream, anoxic treatment to denitrify a waste stream, anoxic treatment to remove selenium and anaerobic treatment to remove heavy metals and sulphur. The process may be used to treat, for example, FGD blow down water. The process may further include one or more of (a) membrane separation of the waste stream upstream of the anoxic digestion to remove selenium, (b) dilution upstream of the biological treatment step, (c) physical/chemical pretreatment upstream of the biological processes or dilution step to remove TSS and soften the waste stream, or (d) ammonia stripping upstream of the biological treatment steps or dilutions step. These processes may be provided in a variety of suspended growth or fixed film reactors, for example a membrane bioreactor or a fixed film reactor having a GAC bed. Processes for biological treatment of inorganic compounds in a fixed medium reactor is described including steps of one or more of maintaining desired ORP levels, optionally by controlling nutrient addition, and removing solids or gas bubbles from the medium bed.
摘要翻译：一个过程有一个或多个需氧处理以除去COD和硝化废物流的一个或多个步骤，对废物流反硝化的缺氧处理，去除硒的缺氧处理以及去除重金属和硫的厌氧处理。该方法可用于处理例如FGD吹扫水。该方法可以进一步包括（a）在缺氧消化上游的废物流的膜分离以除去硒，（b）生物处理步骤上游的稀释，（c）生物过程上游的物理/化学预处理或稀释步骤以去除TSS并软化废物流，或（d）生物处理步骤或稀释步骤上游的氨汽提。这些方法可以在各种悬浮生长或固定膜反应器中提供，例如膜生物反应器或具有GAC床的固定膜反应器。描述了在固定介质反应器中生物处理无机化合物的方法，其包括一个或多个保持所需ORP水平的步骤，任选地通过控制营养添加，以及从中等床除去固体或气泡。

3. 发明申请

US20070102339A1 Membrane filtration apparatus and process optionally for sand filter retrofit 审中-公开
标题翻译：膜过滤装置和工艺任选用于砂过滤器改造
公开(公告)号：US20070102339A1
公开(公告)日：2007-05-10
申请号：US11593001
申请日：2006-11-06
申请人： Pierre Cote , Nicholas Adams
发明人： Pierre Cote , Nicholas Adams
IPC分类号： B01D63/00
CPC分类号： B01D63/046 , B01D61/18 , B01D2313/02 , B01D2313/06 , B01D2313/20 , B01D2313/26 , B01D2315/06 , B01D2317/04 , C02F1/001 , C02F1/444
摘要： A filtration apparatus has a horizontally oriented permeate conduit supported on the floor of a tank. A module of filtering membranes may be placed on or over the permeate conduit and communicate with the permeate conduit. The module may be of a variety of configurations including one with vertically oriented hollow fibers. A permeate collector may be connected to the permeate conduit by a second permeate conduit. The connection may be made near the top of the module and may be through an isolation valve. The apparatus is suitable, among other things, for installation in a sand filter tank. Permeation may be by gravity flow. This abstract is not to be used to construe the claims.
摘要翻译：过滤装置具有支撑在罐的地板上的水平取向的渗透管道。过滤膜的模块可以放置在渗透管道上或上方，并与渗透物导管连通。模块可以是各种配置，包括具有垂直取向的中空纤维的构造。渗透物收集器可以通过第二渗透管道连接到渗透物导管。连接可以靠近模块的顶部，并且可以通过隔离阀。该装置尤其适用于安装在砂滤池中。渗透可能是重力流动。这个摘要不是用来解释权利要求。

4. 发明授权

US07166229B2 Method and apparatus for extracting liquid present in a humid mass 有权
标题翻译：用于提取潮湿物质中存在的液体的方法和装置
公开(公告)号：US07166229B2
公开(公告)日：2007-01-23
申请号：US10481125
申请日：2002-07-05
申请人： Pierre Cote , Michel Fortier , Serge Fournier
发明人： Pierre Cote , Michel Fortier , Serge Fournier
IPC分类号： B01D37/04 , B30B3/04
CPC分类号： B01D33/15 , B01D33/21 , B01D33/466 , B01D33/644 , B01D33/76 , B01D33/808
摘要： A system for extracting a liquid by pressing a humid mass, the system including at least one extraction channel, while extraction channel being provided with at least one inlet allowing to feed the extraction channel with the humid mass to be treated; with walls provided with holes allowing the flow of the liquid contained in the humid mass being pressed, and with at least one outlet allowing the discharge of the dehydrated mass obtained by pressing in the extracting channel, wherein the outlet of the channel, positioned between the walls provided with holes and the exterior, is free of contraints or only includes weak constraints whose level is controlled as a function of physical parameters. This systems is suitable for the efficient continuous dewatering treatment of a feeding source with a composition, consistency and nature of the solid particles present in the feeding source susceptible to vary during the processing.
摘要翻译：一种用于通过冲压潮湿块来提取液体的系统，所述系统包括至少一个提取通道，同时提取通道设置有至少一个入口，允许将所述提取通道供给待处理的湿物质; 其中壁设置有允许湿物质中包含的液体的流动被按压的孔，并且具有至少一个出口，允许通过在提取通道中压制而获得的脱水物质的排出，其中通道的出口位于设有孔和外部的墙壁没有约束，或仅包括其水平受物理参数的影响的弱约束。该系统适用于进料源的有效连续脱水处理，其中存在于进料源中的固体颗粒的组成，稠度和性质易于在加工过程中变化。

5. 发明申请

US20060163157A1 Supported biofilm apparatus and process 有权
公开(公告)号：US20060163157A1
公开(公告)日：2006-07-27
申请号：US11357051
申请日：2006-02-21
申请人： Pierre Cote , Hidayat Husain , Henry Behmann
发明人： Pierre Cote , Hidayat Husain , Henry Behmann
IPC分类号： C02F3/00
CPC分类号： B01D63/02 , B01D63/021 , B01D63/022 , B01D63/04 , B01D69/084 , B01F13/0266 , C02F3/102 , C02F3/103 , C02F3/208 , C02F3/30 , C02F3/302 , C02F2103/005 , C02F2103/008 , Y02W10/15
摘要： A membrane supported biofilm reactor uses modules having fine, hollow fibres, for example, made from melt spun thermoplastic polymers treated after spinning to increase their permeability to oxygen, used, for example, in tows or formed into a fabric. In one module, one or more sheets of the fabric are potted into a module to enable oxygen containing gas to be supplied to the lumens of the hollow fibres. Various reactors and processes, for example to treat wastewater, using such modules are described. In one process, oxygen travels through fibers, optionally through an attached biofilm, to oxygenate surrounding water. Mechanical, chemical and biological methods, for example endogenous respiration, are used to control the thickness of the biofilm.

6. 发明申请

US20060091075A1 Water filtration using immersed membranes 审中-公开
公开(公告)号：US20060091075A1
公开(公告)日：2006-05-04
申请号：US11302271
申请日：2005-12-14
申请人： Pierre Cote , Hidayat Husain
发明人： Pierre Cote , Hidayat Husain
IPC分类号： B01D65/02
CPC分类号： B01D65/08 , B01D61/142 , B01D61/145 , B01D61/147 , B01D61/16 , B01D61/18 , B01D61/22 , B01D63/02 , B01D63/043 , B01D65/02 , B01D2311/04 , B01D2315/06 , B01D2321/04 , B01D2321/16 , B01D2321/185 , B01D2321/2066 , B01D2321/2083 , C02F1/444 , C02F3/1273 , Y02W10/15 , B01D2311/2649 , B01D2311/14 , B01D2311/10 , B01D2311/2661
摘要： A process for operating filtering membranes submerged in a tank involves, in one aspect, periodically deconcentrating the tank by partially emptying and refilling the tank with fresh water. The emptying and refilling may be performed generally simultaneously or sequentially. In another embodiment, the membrane modules are arranged in a series of filtration zones between a feed water inlet and a retentate outlet of a tank and the zone adjacent the outlet is emptied and refilled.

7. 发明申请

US20060054552A1 Membrane bioreactor, process and aerator 审中-公开
公开(公告)号：US20060054552A1
公开(公告)日：2006-03-16
申请号：US11262750
申请日：2005-11-01
申请人： Minggang Liu , Hidayat Husain , Pierre Cote , Ian Pottinger
发明人： Minggang Liu , Hidayat Husain , Pierre Cote , Ian Pottinger
IPC分类号： C02F3/30 , C02F1/74
CPC分类号： C02F3/1215 , B01D61/22 , B01D65/02 , B01D65/08 , B01D2311/2642 , B01D2313/26 , B01D2315/06 , B01D2321/04 , B01D2321/16 , B01D2321/185 , B01D2321/40 , C02F3/1268 , C02F3/1273 , C02F3/302 , C02F2103/002 , C02F2103/005 , C02F2209/42 , Y02W10/15 , Y10S210/903
摘要： A reactor has an aerobic tank, an anoxic tank and a sealed membrane tank with conduits for circulating mixed liquor between them. Permeation starts when the mixed liquor reaches a high level and stops when the mixed liquor reaches a low level. A sensor, for detecting the mixed liquor level, may stop and start permeation. Pressure builds in the membrane tank when membrane air is on. Transmembrane pressure is also provided by gravity flow or siphon. Membrane air generates an air lift which drives the mixed liquor circulation. The total amount of air provided by an air source is divided and varied in time between the membrane aerator and the process aerator. The process aerator acts as a screening inlet to the conduit to the membrane tank. Chemical maintenance cleaning is provided by gravity flow.

8. 发明申请

US20050224412A1 Water treatment system having upstream control of filtrate flowrate and method for operating same 审中-公开
标题翻译：水处理系统具有上游控制滤液流量和操作方法
公开(公告)号：US20050224412A1
公开(公告)日：2005-10-13
申请号：US11101486
申请日：2005-04-08
申请人： Graham Best , Nicholas Adams , Pierre Cote , Daniel Zabarylo
发明人： Graham Best , Nicholas Adams , Pierre Cote , Daniel Zabarylo
IPC分类号： B01D61/14 , B01D61/18 , B01D61/20 , B01D61/22 , C02F1/00 , C02F1/44
CPC分类号： B01D61/142 , B01D61/18 , B01D61/22 , C02F1/008 , C02F1/444 , C02F2301/043
摘要： A method for treating water with a membrane filtration unit provides a generally constant filtrate flowrate from one or more membrane filtration units by varying the pressure on the upstream or feed side of the unit(s) as required by changes in the permeability of the (units).
摘要翻译：用膜过滤单元处理水的方法通过根据需要通过改变单元的渗透性的变化来改变来自一个或多个膜过滤单元的通常恒定的滤液流速）。

9. 发明申请

US20050121389A1 Immersed membrane filtration system and overflow process 有权
标题翻译：浸入膜过滤系统和溢流过程
公开(公告)号：US20050121389A1
公开(公告)日：2005-06-09
申请号：US11038278
申请日：2005-01-21
申请人： Arnold Janson , Nicholas Adams , Jason Cadera , Pierre Cote , Steven Pedersen
发明人： Arnold Janson , Nicholas Adams , Jason Cadera , Pierre Cote , Steven Pedersen
IPC分类号： B01D61/14 , B01D61/18 , B01D63/02 , B01D63/04 , B01D63/16 , B01D65/02 , B01D65/08 , B01D65/10 , C02F1/44
CPC分类号： C02F1/444 , B01D61/145 , B01D61/147 , B01D61/18 , B01D61/20 , B01D63/02 , B01D63/024 , B01D63/026 , B01D63/04 , B01D63/043 , B01D63/16 , B01D65/02 , B01D65/10 , B01D65/104 , B01D2313/06 , B01D2313/54 , B01D2313/56 , B01D2315/06 , B01D2321/185
摘要： Modules of ultrafiltration or microfiltration membranes are arranged in a tank open to the atmosphere to substantially cover the cross sectional area of the tank. A filtration cycle has permeation steps and deconcentration steps. During permeation, supply of feed substantially equals feed removed and little if any aeration is used. During deconcentration, aeration with scouring bubbles is provided with one or both of backwashing and feed flushing. In feed flushing, feed water is supplied to the tank from below the modules. Excess tank water created during deconcentration flows generally upwards through the modules and out through a retentate outlet or overflow at the top of the tank.
摘要翻译：超滤或微滤膜的模块布置在通向大气的罐中，以基本上覆盖罐的横截面积。过滤循环具有渗透步骤和分解步骤。在渗透期间，进料的供给基本上等于进料的去除，如果使用任何通气则很少。在分离浓缩过程中，具有冲洗气泡的曝气提供反冲洗和进料冲洗中的一种或两种。在进料冲洗中，进料水从模块的下方供应到油箱。在分离浓缩过程中产生的过多水箱水通常通过模块向上流出并通过滞留出口溢出或溢出在罐顶部。

10. 发明申请

US20050000895A1 Use of polymer as flocculation aid in membrane filtration 审中-公开
标题翻译：使用聚合物作为膜过滤中的絮凝助剂
公开(公告)号：US20050000895A1
公开(公告)日：2005-01-06
申请号：US10887876
申请日：2004-07-12
申请人： Jason Cadera , Pierre Cote
发明人： Jason Cadera , Pierre Cote
IPC分类号： B01D61/16 , C02F1/00 , C02F1/44 , C02F1/56 , C02F1/66 , C02F9/00 , B01D65/02
CPC分类号： C02F1/444 , B01D61/145 , B01D61/147 , B01D61/16 , B01D2311/04 , B01D2315/06 , C02F1/001 , C02F1/5236 , C02F1/56 , C02F1/66 , C02F9/00 , C02F2209/11 , B01D2311/2642 , B01D2311/2649
摘要： A method of filtering a feed of water to provide potable water includes adding a coagulant to the water to be filtered to encourage the formation of flocs. About 0.1 to 1 mg/L of a polymeric flocculation aid is also added to the water to be filtered to further encourage the formation of flocs. Some of the flocs may then removed from the water to be treated, for example with a clarifier. A filtered permeate is removed from the water to be treated with a membrane filtration device. The membrane filtration device may be an immersed suction driven membrane filtration device. The polymeric flocculation aid may be added to the body of water in a dosage between about 0.2 and 0.5 mg/L. The dosage of the polymeric flocculation aid may also be approximately equal to the dosage which gives the minimum turbidity of the water to be treated, for example, as determined by jar testing.
摘要翻译：过滤水的进料以提供饮用水的方法包括将絮凝剂加入待过滤的水中以促进絮凝物的形成。将约0.1至1mg / L的聚合物絮凝助剂也加入待过滤的水中以进一步促进絮凝物的形成。然后可以将一些絮凝物从待处理的水中除去，例如用澄清池。用膜过滤装置从被处理的水中除去过滤的渗透物。膜过滤装置可以是浸入式抽吸驱动膜过滤装置。聚合物絮凝助剂可以以约0.2至0.5mg / L的剂量加入到水体中。聚合物絮凝助剂的剂量也可以近似等于给出待处理水的最低浊度的剂量，例如通过罐测试测定。

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