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    • 1. 发明申请
    • PRODUCTION LINE AND TREATMENT FOR ORGANIC PRODUCT
    • 生产线和有机产品处理
    • WO2005089513A3
    • 2006-05-18
    • PCT/US2005009312
    • 2005-03-17
    • GE IONICS INCZHANG LIZHENG YONGCHANGMACDONALD RUSSELL JJU ALEX
    • ZHANG LIZHENG YONGCHANGMACDONALD RUSSELL JJU ALEX
    • B01D61/44B01D61/46C12M1/00B01D61/48
    • B01D61/46B01D61/445C07K1/24C12M47/12
    • A fluid from a fermentation process or the like is passed or circulated through chambers of a bipolar membrane electrodialysis unit to separate an ionizable organic acid stream and at least one co-ion or residual stream. The organic acid stream is preferably concentrated (e.g., by recirculation, dewatering or both), and a product is recovered from the concentrated stream, for example by crystallization, and other outputs from the electrodialysis unit may be integrated with overall treatment and applied elsewhere in the treatment system. Depleted feed may be returned upstream to enhance yield, condition the medium or form a by-product. Treatment systems of the invention may replace a cation exchange bed and/or various filter arrangements, and recirculation of the feed and product flows through the unit enhance recovery, separation and quality of the target species. An ED chamber may include a filling of ion exchange beads to maintain a desired operating efficiency as the feed is depleted, and the straight­through operation effectively operates as pre-filtration stage to provide downstream product-bearing flows with processing characteristics for enhanced treatment, recovery and product quality. When operated to treat a downstream waste, systems allow additional recovery of value in the form of product, unexpended nutrients, co-factors and/or other components present in the waste.
    • 来自发酵过程等的流体通过或循环通过双极膜电渗析装置的室,以分离出可电离的有机酸流和至少一种共离子或残余流。 优选浓缩有机酸流(例如通过再循环,脱水或两者),并且例如通过结晶从浓缩物流中回收产物,并且来自电渗析装置的其它输出可以与整体处理相结合并在其它地方应用 治疗系统。 消耗的饲料可以向上游返回以提高产量,调节培养基或形成副产物。 本发明的处理系统可以替代阳离子交换床和/或各种过滤器装置,并且通过该单元的进料和产物流的再循环增强了目标物种的回收,分离和质量。 ED室可以包括填充离子交换珠,以在进料耗尽时保持期望的操作效率,并且直通操作有效地作为预过滤阶段进行运作,以提供具有加工特性的下游产品流动,用于增强处理,回收和 产品质量。 当操作处理下游废物时,系统允许以产品,未用的营养物,辅因子和/或废物中存在的其他成分的形式额外回收价值。
    • 2. 发明申请
    • BIPOLAR MEMBRANE AND METHOD OF MAKING SAME
    • 双极膜及其制造方法
    • WO2006004662A1
    • 2006-01-12
    • PCT/US2005/022737
    • 2005-06-23
    • GE IONICS, INC.ZHENG, YongchangMACDONALD, Russell, J.JU, AlexSIMS, Keith
    • ZHENG, YongchangMACDONALD, Russell, J.JU, AlexSIMS, Keith
    • C25B13/00
    • B01D61/445C08J5/2231C08J5/2275
    • A sheet having anion exchange functionality and a sheet having cation exchange functionality are juxtaposed and joined by current bonding into a unitary bipolar membrane. This may be done without added reactants or bonding agents by placing the two-layer assembly between opposed electrodes in a fluid cell, preferably at pressure, and applying power across the cell to split water in a junction region of the membrane assembly. Preferably the anion exchange sheet is treated with an iron salt solution so as to incorporate or immobilize the metal in the polymer during the current bonding process, and enhance operating characteristics of the bipolar junction. Membrane peel strength is comparable to or greater than that of an underlying sheet of ion exchange material, but the bonding is fully reversible, e.g., by soaking in a concentrated solution. Preferably both sheets include an aromatic backbone or cross-linker component. One membrane may be a self supporting membrane, such as a conventional electrodialysis exchange membrane of 5-50 mil (0.12-1.2 mm) thickness, while the other may also be a commercial membrane of opposite exchange type and of similar strength or thickness, or may be specially manufactured to tailor its performance in the completed membrane. For example, one or both starting sheets may be manufactured with a pore former or may otherwise have its porosity, cross-linking, strength, ion rejection characteristics or thickness tailored for more effective bipolar operation -for example, to enhance transport or diffusion, resist shear or mechanical forces, improve chemical resistance to splitting products or species in the intended feed, or the like. Preferably, prior to contacting and bonding, the anion exchange membrane is treated with a group VIII metal salt. The current-bonded unitary bilayer construction remains contact bonded over its surface and resists degradation in normal use.
    • 具有阴离子交换官能团的片材和具有阳离子交换功能的片材并置并通过电流接合连接成单一双极性膜。 这可以通过将两层组件放置在流体池中的相对电极之间,优选地在压力下,并且跨过电池施加电力以在膜组件的接合区域中分离水来完成,而不需要添加反应物或粘合剂。 优选地,用铁盐溶液处理阴离子交换片,以便在当前的接合过程中将金属掺入或固定在聚合物中,并增强双极结的操作特性。 膜剥离强度与离子交换材料的下层片材的剥离强度相当或更大,但是粘合是完全可逆的,例如通过浸泡在浓缩溶液中。 两片优选包括芳族主链或交联剂组分。 一个膜可以是自支撑膜,例如5-50密耳(0.12-1.2mm)厚度的常规电渗析交换膜,而另一个膜也可以是具有相似交换类型和类似强度或厚度的商业膜,或 可以特别制造以在完成的膜中调整其性能。 例如,一个或两个起始片材可以用成孔剂制造,或者可以具有为更有效的双极操作而定制的孔隙率,交联,强度,离子排斥特性或厚度,例如增强转运或扩散,抗蚀剂 剪切或机械力,提高对预期进料中的分解产物或物质的耐化学性等。 优选地,在接触和接合之前,阴离子交换膜用VIII族金属盐处理。 当前粘合的单层双层结构在其表面保持接触粘合,并在正常使用中抵抗降解。
    • 3. 发明申请
    • PRODUCTION LINE AND TREATMENT FOR ORGANIC PRODUCT
    • 生产线和有机产品处理
    • WO2005089513A2
    • 2005-09-29
    • PCT/US2005/009312
    • 2005-03-17
    • GE IONICS, INC.ZHANG, LiZHENG, YongchangMACDONALD, Russell, J.JU, Alex
    • ZHANG, LiZHENG, YongchangMACDONALD, Russell, J.JU, Alex
    • B01D61/44B01D61/46C12M1/00
    • B01D61/46B01D61/445C07K1/24C12M47/12
    • A fluid from a fermentation process or the like is passed or circulated through chambers of a bipolar membrane electrodialysis unit to separate an ionizable organic acid stream and at least one co-ion or residual stream. The organic acid stream is preferably concentrated (e.g., by recirculation, dewatering or both), and a product is recovered from the concentrated stream, for example by crystallization, and other outputs from the electrodialysis unit may be integrated with overall treatment and applied elsewhere in the treatment system. Depleted feed may be returned upstream to enhance yield, condition the medium or form a by-product. Treatment systems of the invention may replace a cation exchange bed and/or various filter arrangements, and recirculation of the feed and product flows through the unit enhance recovery, separation and quality of the target species. An ED chamber may include a filling of ion exchange beads to maintain a desired operating efficiency as the feed is depleted, and the straight­through operation effectively operates as pre-filtration stage to provide downstream product-bearing flows with processing characteristics for enhanced treatment, recovery and product quality. When operated to treat a downstream waste, systems allow additional recovery of value in the form of product, unexpended nutrients, co-factors and/or other components present in the waste.
    • 来自发酵过程等的流体通过或循环通过双极膜电渗析装置的室,以分离出可电离的有机酸流和至少一种共离子或残余流。 优选浓缩有机酸流(例如通过再循环,脱水或两者),并且例如通过结晶从浓缩物流中回收产物,并且来自电渗析装置的其它输出可以与整体处理相结合并在其它地方应用 治疗系统。 消耗的饲料可以向上游返回以提高产量,调节培养基或形成副产物。 本发明的处理系统可以替代阳离子交换床和/或各种过滤器装置,并且通过该单元的进料和产物流的再循环增强了目标物种的回收,分离和质量。 ED室可以包括填充离子交换珠,以在进料耗尽时保持期望的操作效率,并且直通操作有效地作为预过滤阶段进行运作,以提供具有加工特性的下游产品流动,用于增强处理,回收和 产品质量。 当操作处理下游废物时,系统允许以产品,未用的营养物,辅因子和/或废物中存在的其他成分的形式额外回收价值。
    • 4. 发明申请
    • FOLD PROTECTION FOR SPIRAL WOUND FILTER ELEMENT
    • 螺旋过滤器元件的保护
    • WO2007037939A1
    • 2007-04-05
    • PCT/US2006/035020
    • 2006-09-08
    • GE IONICS, INC.DE LA CRUZ, JoshCHOJNOWSKI, Nick
    • DE LA CRUZ, JoshCHOJNOWSKI, Nick
    • B01D63/10B01D65/00
    • B01D63/103B01D65/003
    • A method for preventing osmotic blistering and other defects in the region of a flex line in a spirally-wound sheet filtration element includes applying an effective glue coating as a sealant to the feedstream side of a sheet in regions where a potential for blistering or layer damage exists, such as a fold line. The glue is applied to the inside of the fold, a spacer is positioned at the coated flex line, and the leaf is refolded and wound with other leaves to form a filter unit, such as a UF, NF or RO filter unit. The coating seals surface defects occurring during the fabrication process as well as the surrounding region, and the cured coating strengthens the region so blistering and delamination do not occur.
    • 在螺旋卷绕片材过滤元件中防止渗透性起泡和弯曲区域中的其它缺陷的方法包括在具有起泡或层损伤的可能性的区域中,在片材的进料流侧施加有效的胶涂层作为密封剂 存在,如折线。 将胶水施加到折叠的内侧,将间隔物定位在涂覆的弯曲线上,并且叶片被折叠并用其它叶片卷绕以形成过滤器单元,例如UF,NF或RO过滤器单元。 涂层密封在制造过程中以及周围区域发生的表面缺陷,并且固化的涂层增强该区域,因此不会发生起泡和分层。
    • 7. 发明专利
    • TREATMENT OF BRINES FOR DEEP WELL INJECTION
    • CA2567171A1
    • 2008-03-22
    • CA2567171
    • 2006-11-03
    • GE IONICS INC
    • HEINS WILLIAM F
    • E21B43/24E21B43/40
    • A process for conditioning of wastewater treatment brines for deep well injection during recovery of heavy hydrocarbon oils in situ. High pressure steam is used to mobilize oil, which is recovered in a mixture of oil and produced water. The produced water is pre-treated by removing residual oil. The remaining water is acidified and steam stripped to remove non-hydroxide alkalinity and non- condensable gases, and is then fed to a crystallizing evaporator, where it i s evaporated from a circulating brine slurry to produce (1) a distillate strea m having a trace amount of residual solutes, and (2) evaporator blowdown stream containing, as dissolved or suspended solids, substantially all of the solut es from the produced water feed. The distillate stream is used as boiler feedwater, either directly or after polishing. The evaporator blowdown is conditioned to remov e substantially all suspended solids and to produce a clear brine solution for deep well injection.