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1.发明申请公开(公告)号：US20110131994A1
公开(公告)日：2011-06-09
申请号：US12631248
申请日：2009-12-04
申请人： Neil Edwin Moe
发明人： Neil Edwin Moe
CPC分类号： F03G7/005 , C02F1/441 , C02F1/4693 , C02F2303/10 , Y02A20/131 , Y02A20/134 , Y02E10/36 , Y02W10/30 , Y10T137/0324
摘要： A method and apparatus are described for disposing of salt byproduct from a zero liquid operation, such as a zero liquid discharge desalination plant. The present method and apparatus concern a power generation plant, comprising a salinity gradient power unit (SGPU) comprising a high salinity feed, a low salinity feed, and a mixed water output. The high salinity feed is comprised of salt byproduct from a ZLD operation. The mixed water output empties into a body of water.
摘要翻译： 描述了用于从零液体操作（例如零液体排放淡化设备）处理盐副产物的方法和装置。 本发明的方法和装置涉及发电设备，其包括含有高盐度进料，低盐度进料和混合水输出的盐度梯度功率单元（SGPU）。 高盐度饲料由ZLD操作的盐副产物组成。 混合水输出排入水体。
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公开(公告)号：US20080000809A1
公开(公告)日：2008-01-03
申请号：US11479322
申请日：2006-06-30
CPC分类号： C10G31/11 , B01D61/025 , B01D61/027 , B01D61/145 , B01D61/147 , B01D61/58
摘要： A method of removing an oil-soluble metal from a hydrocarbon feedstock comprises passing the hydrocarbon feedstock through a nanofiltration membrane or a reverse osmosis membrane to produce a permeate stream having at least a vanadium concentration less than an initial vanadium concentration in the hydrocarbon feedstock, and a retentate stream having at least a vanadium concentration greater than the initial vanadium concentration in the hydrocarbon feedstock.
摘要翻译： 从烃原料中除去油溶性金属的方法包括使烃原料通过纳滤膜或反渗透膜，以产生至少钒浓度低于烃原料中的初始钒浓度的渗透物流，以及 具有至少钒浓度大于烃原料中的初始钒浓度的滞留物料流。
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公开(公告)号：US09382135B2
公开(公告)日：2016-07-05
申请号：US13267553
申请日：2011-10-06
申请人： Neil Edwin Moe , John Barber
发明人： Neil Edwin Moe , John Barber
CPC分类号： C02F1/441 , C02F1/042 , C02F1/4695 , C02F2103/08 , C02F2303/10 , C02F2303/22 , Y02A20/128 , Y02A20/131 , Y02A20/134 , Y02W10/30
摘要： In a desalination system, water is treated, for example by reverse osmosis, to produce desalinated product water and a reject stream. Salt from the reject stream is transferred to a flow of low salinity wastewater, such as effluent from a municipal wastewater treatment plant. For example, the reject stream may be fed to the high salinity cell in an electrodialysis (ED) unit. The adjacent low salinity cell receives the low salinity wastewater. The high salinity and low salinity cells are separated by ion exchange membranes. The salty wastewater is discharged, for example to the ocean. The salt-reduced reject stream is treated to extract more product water from it, for example by recycling it to the feed water. Less feed water is needed to produce a given volume of product water. If a thermal desalination unit is combined with divalent ion selective ion exchange membranes, then scaling is reduced.
摘要翻译： 在脱盐系统中，例如通过反渗透处理水，以产生脱盐产物水和废水。 来自废弃物流的盐被转移到低盐度废水流中，例如来自市政废水处理厂的废水。 例如，废电流可以在电渗析（ED）单元中供给到高盐度电池。 相邻的低盐度细胞接收低盐度废水。 高盐度和低盐度的细胞由离子交换膜分离。 咸水被排放到例如海洋。 处理减盐废液流以从其中提取更多的产物水，例如通过将其再循环到给水中。 产生一定体积的产品水需要较少的给水。 如果热脱盐单元与二价离子选择性离子交换膜结合，则缩小。
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公开(公告)号：US20130087501A1
公开(公告)日：2013-04-11
申请号：US13267553
申请日：2011-10-06
申请人： Neil Edwin MOE , John BARBER
发明人： Neil Edwin MOE , John BARBER
CPC分类号： C02F1/441 , C02F1/042 , C02F1/4695 , C02F2103/08 , C02F2303/10 , C02F2303/22 , Y02A20/128 , Y02A20/131 , Y02A20/134 , Y02W10/30
摘要： In a desalination system, water is treated, for example by reverse osmosis, to produce desalinated product water and a reject stream. Salt from the reject stream is transferred to a flow of low salinity wastewater, such as effluent from a municipal wastewater treatment plant. For example, the reject stream may be fed to the high salinity cell in an electrodialysis (ED) unit. The adjacent low salinity cell receives the low salinity wastewater. The high salinity and low salinity cells are separated by ion exchange membranes. The salty wastewater is discharged, for example to the ocean. The salt-reduced reject stream is treated to extract more product water from it, for example by recycling it to the feed water. Less feed water is needed to produce a given volume of product water. If a thermal desalination unit is combined with divalent ion selective ion exchange membranes, then scaling is reduced.
摘要翻译： 在脱盐系统中，例如通过反渗透处理水，以产生脱盐产物水和废水。 来自废弃物流的盐被转移到低盐度废水流中，例如来自市政废水处理厂的废水。 例如，废电流可以在电渗析（ED）单元中供给到高盐度电池。 相邻的低盐度细胞接收低盐度废水。 高盐度和低盐度的细胞由离子交换膜分离。 咸水被排放到例如海洋。 处理减盐废液流以从其中提取更多的产物水，例如通过将其再循环到给水中。 产生一定体积的产品水需要较少的给水。 如果热脱盐单元与二价离子选择性离子交换膜结合，则缩小。
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公开(公告)号：US07642393B2
公开(公告)日：2010-01-05
申请号：US11543363
申请日：2006-10-05
IPC分类号： C07C7/144
CPC分类号： C10G21/06 , B01D61/246 , B01D61/362 , C10G31/11 , C10G45/44 , C10G53/04 , C10G67/14 , Y10S203/20
摘要： A method of removing at least benzene from a hydrocarbon stream comprises concentrating aromatics in the hydrocarbon stream by passing the hydrocarbon stream through a membrane unit having at least one membrane to produce a permeate stream and a retentate stream, wherein the permeate stream is aromatics rich relative to the hydrocarbon stream; and extracting aromatics after concentrating using a selective aromatics extraction solvent in an extraction unit to produce an extract stream, wherein the extract stream is aromatics rich relative to the permeate stream.
摘要翻译： 从烃流中至少除去苯的方法包括通过使烃流通过具有至少一个膜的膜单元以产生渗透物流和滞留物流来将芳烃浓缩在烃流中，其中渗透物流是富含芳烃的相对 到烃流; 并且在萃取单元中使用选择性芳族化合物萃取溶剂浓缩后提取芳族化合物以产生萃取物流，其中提取物物流相对于渗透物流富含芳烃。
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公开(公告)号：US20090223229A1
公开(公告)日：2009-09-10
申请号：US11612760
申请日：2006-12-19
CPC分类号： B01D53/228 , B01D2256/20 , B01D2257/102 , F02C3/30 , F02C3/305 , F05D2220/75 , F05D2260/211 , F23K5/002 , F23K2401/10 , Y02E20/16 , Y02T50/675
摘要： In one embodiment, a combustion system comprises: a fuel supply comprising a fuel having a heating value of less than or equal to about 100 Btu/scf, an inert gas sequestration unit in fluid communication with the fuel supply, and a combustion system located downstream of and in fluid communication with the inert gas sequestration unit and with an oxidant supply. The inert gas sequestration unit comprises a membrane configured to separate N2 from CO and to form a retentate stream having a heating value of greater than or equal to about 110 Btu/scf. In one embodiment, a method for operating a power plant, comprises: passing a fuel stream through an inert gas sequestration unit to remove N2 from the fuel stream and to form a retentate stream, and combusting the retentate stream and an oxidant stream to form a combustion stream.
摘要翻译： 在一个实施方案中，燃烧系统包括：燃料供应，其包括具有小于或等于约100Btu / scf的加热值的燃料，与燃料供应流体连通的惰性气体封存单元和位于下游的燃烧系统 与惰性气体封存单元和与氧化剂供应流体连通。 惰性气体封存单元包括被配置为将N 2与CO分离并形成具有大于或等于约110Btu / scf的加热值的滞留物流的膜。 在一个实施例中，一种用于操作发电厂的方法包括：使燃料流通过惰性气体封存单元以从燃料流中除去N 2并形成滞留物流，并且燃烧滞留物流和氧化剂流以形成 燃烧流。
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公开(公告)号：US09339765B2
公开(公告)日：2016-05-17
申请号：US13234232
申请日：2011-09-16
申请人： Neil Edwin Moe
发明人： Neil Edwin Moe
CPC分类号： B01D61/46 , B01D61/025 , B01D61/44 , B01D61/58 , C02F1/4693
摘要： In one embodiment, this invention relates to an electrodialysis device comprising an inlet for directing a feed stream into a plurality of first feed paths and a plurality of second feed paths; the feed stream is comprised of a first anionic scaling species and a first cationic scaling species; the first cationic scaling species is transferred from the second feed paths to the first feed paths through a first membrane group, the first anionic scaling species is transferred from the first feed paths to the second feed paths through the first membrane group. In another embodiment, this invention relates to a method for passivating scaling species in an electrodialysis device.
摘要翻译： 在一个实施例中，本发明涉及电渗析装置，其包括用于将进料流引导到多个第一进料路径和多个第二进料路径的入口; 进料流由第一阴离子结垢物质和第一阳离子结垢物质组成; 第一阳离子结垢物质从第二进料路径通过第一膜组转移到第一进料路径，第一阴离子结垢物质从第一进料路径转移到通过第一膜组的第二进料路径。 在另一个实施方案中，本发明涉及一种用于钝化电渗析装置中的结垢物质的方法。
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8.发明申请公开(公告)号：US20140102980A1
公开(公告)日：2014-04-17
申请号：US14123302
申请日：2012-06-01
CPC分类号： C02F9/00 , B01J41/12 , B01J49/07 , B01J49/57 , B01J49/70 , C02F1/42 , C02F1/44 , C02F1/441 , C02F1/442 , C02F1/4693 , C02F3/2833 , C02F3/34 , C02F2001/422 , C02F2101/12 , C02F2201/46115 , C02F2201/4613 , C02F2201/4618 , C02F2303/16
摘要： A process and apparatus treat brackish or non-brackish waters containing an oxidant such as perchlorate. The feed water is converted into a treated water stream and a concentrate stream in an ED, EDR, NF or RO unit. The concentrate passes through an IX resin. The IX resin removes oxidant from the concentrate stream to produce a second treated water stream. The IX resin is periodically regenerated, for example biologically in a fluidised bed reactor in regeneration system. Concentrate that has passed through the IX resin has a reduced concentration of oxidant, preferably a concentration safe for discharge or use. In the case of a brackish feed water, the second treated water stream may be desalted.
摘要翻译： 处理和装置处理含有氧化剂如高氯酸盐的咸水或非咸水。 将进料水转化为ED，EDR，NF或RO单元中的处理水流和浓缩物流。 浓缩物通过IX树脂。 IX树脂从浓缩物流中除去氧化剂以产生第二处理水流。 IX再生系统周期性再生，例如生物地在流化床反应器中再生。 已经通过IX树脂的浓缩物具有降低的氧化剂浓度，优选为排放或使用安全的浓度。 在微咸水的情况下，第二处理水流可以脱盐。
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公开(公告)号：US20130068620A1
公开(公告)日：2013-03-21
申请号：US13234232
申请日：2011-09-16
申请人： Neil Edwin Moe
发明人： Neil Edwin Moe
CPC分类号： B01D61/46 , B01D61/025 , B01D61/44 , B01D61/58 , C02F1/4693
摘要： In one embodiment, this invention relates to an electrodialysis device comprising an inlet for directing a feed stream into a plurality of first feed paths and a plurality of second feed paths; the feed stream is comprised of a first anionic scaling species and a first cationic scaling species; the first cationic scaling species is transferred from the second feed paths to the first feed paths through a first membrane group, the first anionic scaling species is transferred from the first feed paths to the second feed paths through the first membrane group. In another embodiment, this invention relates to a method for passivating scaling species in an electrodialysis device.
摘要翻译： 在一个实施例中，本发明涉及电渗析装置，其包括用于将进料流引导到多个第一进料路径和多个第二进料路径的入口; 进料流由第一阴离子结垢物质和第一阳离子结垢物质组成; 第一阳离子结垢物质从第二进料路径通过第一膜组转移到第一进料路径，第一阴离子结垢物质从第一进料路径转移到通过第一膜组的第二进料路径。 在另一个实施方案中，本发明涉及一种用于钝化电渗析装置中的结垢物质的方法。
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10.发明授权公开(公告)号：US08695343B2
公开(公告)日：2014-04-15
申请号：US12631248
申请日：2009-12-04
申请人： Neil Edwin Moe
发明人： Neil Edwin Moe
IPC分类号： F01K25/06
CPC分类号： F03G7/005 , C02F1/441 , C02F1/4693 , C02F2303/10 , Y02A20/131 , Y02A20/134 , Y02E10/36 , Y02W10/30 , Y10T137/0324
摘要： A method and apparatus are described for disposing of salt byproduct from a zero liquid operation, such as a zero liquid discharge desalination plant. The present method and apparatus concern a power generation plant, comprising a salinity gradient power unit (SGPU) comprising a high salinity feed, a low salinity feed, and a mixed water output. The high salinity feed is comprised of salt byproduct from a ZLD operation. The mixed water output empties into a body of water.
摘要翻译： 描述了用于从零液体操作（例如零液体排放淡化设备）处理盐副产物的方法和装置。 本发明的方法和装置涉及发电设备，其包括含有高盐度进料，低盐度进料和混合水输出的盐度梯度功率单元（SGPU）。 高盐度饲料由ZLD操作的盐副产物组成。 混合水输出排入水体。
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