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公开(公告)号：US09061250B2
公开(公告)日：2015-06-23
申请号：US13380393
申请日：2010-06-25
IPC分类号： B01D39/00 , B01D39/14 , B29C47/00 , B29C47/12 , B29C47/88 , D01D5/08 , B01D69/02 , B01D69/08
CPC分类号： B01D69/02 , B01D69/08 , B01D69/085 , B01D69/087 , B01D2323/39 , B01D2323/42 , B01D2325/40 , B29C47/0014 , B29C47/0021 , B29C47/0028 , B29C47/003
摘要： Various methods of making a reinforced membrane, devices for making the membranes, and the resulting membranes are described. The methods typically provide a reinforcing structure that includes filaments extending around the circumference of the membrane but without the filaments being part of a braided or woven structure. Some of the reinforcing structures also include longitudinal filaments. The methods and devices can be used to make a supporting structure in line with membrane formation steps, and also allow for a reinforced membrane to be produced that has a ratio of inside-to-outside diameters of 0.5 or more.
摘要翻译： 描述制造增强膜的各种方法，制造膜的装置以及所得的膜。 该方法通常提供一种加强结构，其包括围绕膜的圆周延伸的细丝，但是丝不是编织或编织结构的一部分。 一些加固结构还包括纵向长丝。 该方法和装置可以用于制造符合膜形成步骤的支撑结构，并且还允许制造具有0.5至更大的内外径比的增强膜。
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公开(公告)号：US20090117631A1
公开(公告)日：2009-05-07
申请号：US12259788
申请日：2008-10-28
摘要： This document describes a fermentation product producing or processing apparatus or process involving membrane pervaporation (PV) and either vapor permeation or distillation or both. The fermentation product may be produced semi-continuously wherein product concentration is maintained below a selected value by removal through pervaporation membranes. After a period of operation, the broth may be distilled. Distillation and/or pervaporation products may be further dewatered using vapor permeation. The PV membranes may be used in the form of immersed modules, for example with a flat sheet configuration.
摘要翻译： 本文件描述了涉及膜渗透蒸发（PV）和蒸气渗透或蒸馏或两者的发酵产物生产或加工设备或方法。 可以半连续地制备发酵产物，其中通过渗透蒸发膜除去产物浓度保持在选定值以下。 经过一段时间后，可以蒸馏肉汤。 可以使用蒸气渗透进一步脱水和/或渗透蒸发产物。 PV膜可以以浸没的模块的形式使用，例如具有平板配置。
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公开(公告)号：US07087173B2
公开(公告)日：2006-08-08
申请号：US10841440
申请日：2004-05-10
CPC分类号： B01D65/08 , B01D61/18 , B01D61/20 , B01D63/021 , B01D63/022 , B01D63/023 , B01D63/026 , B01D63/043 , B01D65/02 , B01D2315/06 , B01D2321/185 , C02F1/444 , C02F3/20 , C02F2303/16 , Y02W10/15
摘要： An aerator for immersed filtering membranes has an aerator shell with openings for discharging bubbles from its upper surface and a shape capable of temporarily containing a volume of air in fluid communication with the openings. The shell is open to tank water below it and located so that discharged bubbles will rise through an assembly of the filtering membranes. The shell may be wholly or partially made of parts of the assemblies of filtering membranes. A supply of air is provided to the air space in the aerators alternating between a high flow rate and a low flow rate in short cycles of between about 10 seconds and 100 seconds. A filtration system has an inlet for adding substrate and an outlet for retentate are located so as to create a horizontal flow of substrate through the tank. Membrane assemblies are located within the horizontal flow of substrate. Aerators as described above are provided and operated as described above.
摘要翻译： 用于浸渍过滤膜的曝气器具有曝气器壳体，其具有用于从其上表面排出气泡的开口和能够临时容纳与开口流体连通的空气量的形状。 壳体对其下方的罐水开放，并且定位成使得排出的气泡将通过过滤膜的组件而上升。 壳体可以全部或部分地由过滤膜组件的部分制成。 在约10秒至100秒之间的短循环中，在高流量和低流量之间交替的通气器中的空气空间供应空气。 过滤系统具有用于添加基底的入口和用于滞留物的出口，以便通过罐产生基底的水平流动。 膜组件位于衬底的水平流动之内。 如上所述提供和操作如上所述的充气器。
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公开(公告)号：US06899811B2
公开(公告)日：2005-05-31
申请号：US10790239
申请日：2004-03-02
IPC分类号： B01D61/18 , B01D61/20 , B01D63/02 , B01D63/04 , B01D65/08 , C02F1/44 , C02F1/74 , B01D63/00 , B01D33/00
CPC分类号： C02F1/444 , B01D61/18 , B01D61/20 , B01D63/02 , B01D63/024 , B01D63/026 , B01D63/043 , B01D63/046 , B01D65/08 , B01D2313/06 , B01D2313/21 , B01D2313/54 , B01D2313/56 , B01D2315/06 , B01D2321/12 , B01D2321/185 , C02F1/74
摘要： An apparatus for filtering a liquid in a tank has a plurality of elements and a frame for holding the elements while they are immersed in the liquid. The elements have a plurality of hollow fibre membranes attached to and suspended between an upper header and a lower header. The membranes are in fluid communication with one or more permeate channels in one or more of the headers. Releasable attachments between the headers and the frame allow the frame to releasably hold the elements by their headers. The size and configuration of the frame determines the positions of the upper and lower headers of each element relative to each other. Connections between the permeate channels and one or more permeate collection tubes attached to the frame are releasable and resealable connections which are made or broken automatically by the movements involved in inserting or removing an element into or out of the frame.
摘要翻译： 用于过滤液体中的液体的装置具有多个元件和用于在元件浸入液体中时保持元件的框架。 这些元件具有多个中空纤维膜，该多个中空纤维膜附着到并悬置在上部集管和下部集管之间。 膜与一个或多个集管中的一个或多个渗透通道流体连通。 头部和框架之间的可释放附件允许框架通过其头部可释放地保持元件。 框架的尺寸和结构决定了每个元件的上下标头相对于彼此的位置。 渗透通道与附着在框架上的一个或多个渗透物收集管之间的连接是可释放和可再密封的连接，其通过将元件插入或移出框架所涉及的移动自动或断开而形成或断开。
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公开(公告)号：US06214231B1
公开(公告)日：2001-04-10
申请号：US09384638
申请日：1999-08-27
IPC分类号： B01D6502
CPC分类号： B01D65/102 , B01D61/142 , B01D61/18 , B01D61/22 , B01D63/043 , B01D63/046 , B01D65/02 , B01D2313/125 , B01D2313/54 , B01D2315/06 , B01D2321/04 , B01D2321/16 , B01D2321/2066 , C02F1/444
摘要： Limitation of the number of cassettes in an assembly currently used for the production of permeate is obviated by grouping plural cassettes into racks one or more of which may be isolated while permeate production from the remaining racks is uninterrupted. Ancillary functions such as back-pulsing, chemical cleaning and testing for defects in membranes (“integrity testing”) in one or more racks may proceed while production of permeate continues. The number of racks in a bank is determined by the period of the overall filtration cycle, typically 15 min, in which filtration period the ancillary period is a minor portion, typically 30 sec. The racks make it possible to use automatic on/off valves which open and close quicker than larger ones. The resulting saving in time, energy, and equipment costs, which when back-pulsing with permeate is surprisingly economical, is even greater when a chemical cleaning solution is to be used. In addition, the saving in cost of equipment and avoiding the wear and tear of pumps which are intermittently stopped and started, produces unexpected economic benefits. For even greater savings in operating costs, a bank of cassettes, or a bank of racks may be operated with a “gravity flow” system.
摘要翻译： 目前用于生产渗透物的组件中的盒的数量的限制是通过将多个盒分组成机架而消除的，其中一个或多个可以被隔离，而从其余的机架产生的渗透物不间断。 在一个或多个机架中的辅助功能如反脉冲，化学清洗和膜缺陷测试（“完整性测试”）可以进行，同时渗透物的生产继续进行。 银行中的货架数量由整个过滤周期的周期确定，通常为15分钟，其中过滤周期的辅助周期是次要的，通常为30秒。 机架使得可以使用比较大的开启和关闭更快的自动开关阀。 当使用化学清洗溶液时，与渗透物反向脉冲相比，由此节省时间，能量和设备成本是惊人的经济性，甚至更大。 此外，节省设备成本，避免间歇停止和启动的泵的磨损，产生意想不到的经济效益。 为了更加节省运营成本，可以使用“重力流”系统操作一盒纸盒或一组机架。
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公开(公告)号：US20080203019A1
公开(公告)日：2008-08-28
申请号：US12120102
申请日：2008-05-13
申请人： Nicholas William Harcsar Adams , Manwinder Singh , Kevin Simon Joseph Dufresne , Pierre Lucien Cote
发明人： Nicholas William Harcsar Adams , Manwinder Singh , Kevin Simon Joseph Dufresne , Pierre Lucien Cote
CPC分类号： B01D65/02 , B01D61/22 , B01D2315/20 , C02F1/44 , C02F2303/16
摘要： A membrane batch filtration process has a step of reducing the water level in the tank by permeation prior to emptying the tank to reduce the volume of water drained after each batch. Permeation may continue even after a portion of the membranes is exposed to air to further lower the water level. The membranes may be backwashed after the water level has been lowered. The water level may be lowered again after the backwash. The tank drain may begin with a portion of the membranes exposed to air.
摘要翻译： 膜批过滤方法具有在排空罐之前通过渗透减少罐中的水位以减少每批后排出的水的体积的步骤。 即使在将一部分膜暴露于空气中以进一步降低水位之后，渗透也可以继续。 在水位降低后，膜可能被反洗。 反冲洗后水位再次下降。 罐排水可以从暴露于空气中的膜的一部分开始。
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公开(公告)号：US20110042312A1
公开(公告)日：2011-02-24
申请号：US12861206
申请日：2010-08-23
CPC分类号： C02F1/444 , B01D61/18 , B01D61/22 , B01D65/02 , B01D65/08 , B01D2315/06 , B01D2321/00 , B01D2321/04 , B01D2321/16 , B01D2321/185 , C02F3/1268 , Y02W10/15
摘要： An immersed membrane system or process may use measured or calculated process information to optimize one or more process operating parameters to improve performance or reduce operating costs. An on-line process control system or method may use the resistance in series method in operating an immersed membrane water treatment system. A process control system or process may consider resistance values and adjust operational parameters such as membrane aeration frequency factor, membrane aeration flow, permeate flux, permeation duration, backwash flow and duration, relaxation duration or maintenance or recovery chemical cleaning frequencies in order to reduce the operational costs related to membrane fouling removal.
摘要翻译： 浸入的膜系统或过程可以使用测量或计算的过程信息来优化一个或多个过程操作参数以改善性能或降低操作成本。 在线过程控制系统或方法可以使用串联方法来操作浸入式膜水处理系统。 过程控制系统或过程可以考虑电阻值并调整操作参数，例如膜曝气频率因子，膜曝气流量，渗透通量，渗透持续时间，反冲洗流量和持续时间，松弛持续时间或维持或恢复化学清洗频率，以便减少 与膜污染去除相关的运营成本。
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公开(公告)号：US09783434B2
公开(公告)日：2017-10-10
申请号：US12861206
申请日：2010-08-23
CPC分类号： C02F1/444 , B01D61/18 , B01D61/22 , B01D65/02 , B01D65/08 , B01D2315/06 , B01D2321/00 , B01D2321/04 , B01D2321/16 , B01D2321/185 , C02F3/1268 , Y02W10/15
摘要： An immersed membrane system or process may use measured or calculated process information to optimize one or more process operating parameters to improve performance or reduce operating costs. An on-line process control system or method may use the resistance in series method in operating an immersed membrane water treatment system. A process control system or process may consider resistance values and adjust operational parameters such as membrane aeration frequency factor, membrane aeration flow, permeate flux, permeation duration, backwash flow and duration, relaxation duration or maintenance or recovery chemical cleaning frequencies in order to reduce the operational costs related to membrane fouling removal.
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公开(公告)号：US08357299B2
公开(公告)日：2013-01-22
申请号：US11484815
申请日：2006-07-11
IPC分类号： B01D61/00
CPC分类号： C02F1/444 , B01D61/18 , B01D61/22 , B01D65/02 , B01D65/08 , B01D2315/06 , B01D2321/00 , B01D2321/04 , B01D2321/16 , B01D2321/185 , C02F3/1268 , Y02W10/15
摘要： An immersed membrane system or process may use measured or calculated process information to optimize one or more process operating parameters to improve performance or reduce operating costs. An on-line process control system or method may use the resistance in series method in operating an immersed membrane water treatment system. A process control system or process may consider resistance values and adjust operational parameters such as membrane aeration frequency factor, membrane aeration flow, permeate flux, permeation duration, backwash flow and duration, relaxation duration or maintenance or recovery chemical cleaning frequencies in order to reduce the operational costs related to membrane fouling removal.
摘要翻译： 浸入的膜系统或过程可以使用测量或计算的过程信息来优化一个或多个过程操作参数以改善性能或降低操作成本。 在线过程控制系统或方法可以使用串联方法来操作浸入式膜水处理系统。 过程控制系统或过程可以考虑电阻值并调整操作参数，例如膜曝气频率因子，膜曝气流量，渗透通量，渗透持续时间，反冲洗流量和持续时间，松弛持续时间或维持或恢复化学清洗频率，以便减少 与膜污染去除相关的运营成本。
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公开(公告)号：US07459076B2
公开(公告)日：2008-12-02
申请号：US11642544
申请日：2006-12-21
申请人： Pierre Lucien Cote , Henry Behmann
发明人： Pierre Lucien Cote , Henry Behmann
IPC分类号： B01D24/00
CPC分类号： C02F3/301 , C02F3/223 , C02F2203/004 , Y02W10/15
摘要： A continuous flow reactor or method promotes aerobic granule formation. The reactor may comprise three or four zones that may comprise one or more of an aerobic zone, an alternately aerobic and anoxic zone or discrete aerobic and anoxic zones, and a settling zone. The reactor may have a single sludge removal flow. An anaerobic zone may be located at the bottom of a mass of settled granules. Feed may be introduced through the settled granules generally in a plug flow. An aerobic/anoxic zone may be structured or operated partially like a continuously stirred tank reactor (CSTR) but with aeration varying in space or time. Sludge granules may move intermittently from an aerobic zone to an aerobic/anoxic zone, for example by an air lift pump. A settling zone may have an upflow of >4 m/hr or >5 m/hr and wash off flocculated biomass.
摘要翻译： 连续流动反应器或方法促进好氧颗粒形成。 反应器可以包括三个或四个区域，其可以包括好氧区，交替需氧和缺氧区或离散的需氧和缺氧区中的一个或多个，以及沉降区。 反应器可以具有单个污泥去除流。 厌氧区可能位于大量沉降颗粒的底部。 进料可以通过沉淀的颗粒通常以活塞流引入。 有氧/缺氧区域可以像连续搅拌的罐式反应器（CSTR）一样构造或部分运行，但是在空间或时间上具有变化的曝气。 污泥颗粒可以从好氧区间歇地移动到需氧/缺氧区域，例如通过空气提升泵。 沉降区可以具有> 4m / hr或> 5m / hr的上流，并且清除絮凝生物质。
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