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    • 4. 发明申请
    • SOLID ELECTROLYTE PRODUCING ASSEMBLY AND METHOD
    • 固体电解液生产组装及方法
    • US20110042232A1
    • 2011-02-24
    • US12544617
    • 2009-08-20
    • Wei CaiRihua XiongChang WeiRobert Lee SolomonRengarajan Ramesh
    • Wei CaiRihua XiongChang WeiRobert Lee SolomonRengarajan Ramesh
    • B01D59/40C25B15/08H01G9/00
    • C02F1/4691C02F1/001C02F1/008C02F1/38C02F1/385C02F1/44C02F1/444C02F1/4604C02F9/00C02F2001/007C02F2001/5218C02F2103/08C02F2201/46195C02F2301/08Y02A20/131
    • A solid electrolyte producing system includes a supercapacitor desalination device comprising a power supply and a supercapacitor desalination unit. The supercapacitor desalination unit includes a pair of electrodes electrically coupled to the power supply and operable in a charging mode of operation and a discharging mode of operation. A feeding source is configured to provide a feed liquid to the supercapacitor desalination unit when the supercapacitor desalination unit is in the charging mode of operation. The feed liquid comprises at least one determined electrolyte. A crystallization device is providing for receiving a concentrated liquid from the supercapacitor desalination device in the discharging mode of operation, the concentrated liquid being a saturated liquid or supersaturated liquid of the at least one determined type of electrolyte. The at least one determined type of electrolyte precipitates in the crystallization device as solid electrolyte. The system further comprises a separation device for separating the solid electrolyte from the liquid of the crystallization device as a solid electrolyte product.
    • 一种固体电解质生产系统,包括包括电源和超级电容器脱盐单元的超级电容器脱盐装置。 超级电容器脱盐单元包括电耦合到电源并可在充电操作模式和放电操作模式下操作的一对电极。 供电源被配置为当超级电容器脱盐单元处于充电操作模式时,向超级电容器脱盐单元提供进料液体。 进料液体包含至少一种确定的电解质。 结晶装置提供在排放操作模式中从超级电容器脱盐装置接收浓缩液体,浓缩液体是至少一种确定类型的电解质的饱和液体或过饱和液体。 所述至少一种确定类型的电解质在所述结晶装置中沉淀为固体电解质。 该系统还包括用于将固体电解质与作为固体电解质产物的结晶装置的液体分离的分离装置。
    • 9. 发明申请
    • DESALINATION SYSTEM AND METHOD
    • 脱盐系统和方法
    • US20140209462A1
    • 2014-07-31
    • US14342936
    • 2012-08-13
    • Rihua XiongLinglu Yang
    • Rihua XiongLinglu Yang
    • C02F1/469
    • C02F1/4695B01D61/44B01D61/48B01D61/58B01D2311/04B01D2311/12C02F1/4602C02F1/4693C02F9/00C02F2201/4611C02F2201/46115C02F2301/08C02F2303/22Y02A20/134
    • A desalination system is provided. The desalination system comprises a desalination apparatus. The desalination apparatus comprises first and second electrodes, and a first group of paired ion exchange membranes disposed between the first and second electrodes to form a first group of alternating first and second channels. The first channels are configured to receive a first stream for desalination and the second channels are configured to receive a second stream to carry away ions removed from the first stream, respectively. The desalination apparatus further comprises a plurality of spacers disposed between each pair of the adjacent ion exchange membranes and between the first and second electrodes and the respective ion exchange membranes. Wherein each of the ion exchange membranes in the first group is a cation exchange membrane. A desalination system and a method for removing ions from an aqueous stream area also presented.
    • 提供脱盐系统。 脱盐系统包括脱盐装置。 脱盐装置包括第一和第二电极以及设置在第一和第二电极之间的第一组成对的离子交换膜,以形成第一组交替的第一和第二通道。 第一通道被配置为接收用于脱盐的第一流,并且第二通道被配置为分别接收第二流以携带从第一流移除的离子。 脱盐装置还包括设置在每对相邻离子交换膜之间以及在第一和第二电极与各离子交换膜之间的多个间隔物。 其中第一组中的每个离子交换膜是阳离子交换膜。 还提出了一种脱盐系统和从水流区域中去除离子的方法。
    • 10. 发明授权
    • Electrochemical desalination system and method
    • 电化学脱盐系统及方法
    • US08663445B2
    • 2014-03-04
    • US12570227
    • 2009-09-30
    • Ran NiuHai YangJohn H. BarberMin HuRihua XiongWei CaiXin GaoYufeng Liu
    • Ran NiuHai YangJohn H. BarberMin HuRihua XiongWei CaiXin GaoYufeng Liu
    • B01D57/00
    • C02F1/4691C02F2103/08C02F2201/46135C02F2201/4614C02F2209/005
    • An electrochemical desalination system includes a first and a second electrochemical device and a controller. The first and second electrochemical devices each comprises a electrochemical desalination module comprising at least one pair of electrodes and a compartment between each pair of electrodes for receiving an electrolyte solution. Each of the first and second electrochemical desalination devices comprises a plurality of successive operation cycles. Each cycle comprises a charging mode of operation for charging each pair of electrodes and for adsorbing ions in the electrolyte solution on the electrodes, and a discharging mode of operation for discharging the pair of electrodes and for desorbing ions from the pair of electrodes. The controller is configured to control the system that the first and second electrochemical desalination devices have interleaved charging and discharging modes of operation. One of the first and second electrochemical desalination devices is in a discharging mode and the at least one pair of electrodes release electrical current, while the other of the first and second electrochemical desalination devices is in a charging mode of operation and receives the electrical current released from said one of the first and second electrochemical desalination device.
    • 电化学脱盐系统包括第一和第二电化学装置和控制器。 第一和第二电化学装置各自包括电化学脱盐模块,其包括至少一对电极和用于接收电解质溶液的每对电极之间的隔室。 第一和第二电化学脱盐装置中的每一个包括多个连续的操作循环。 每个循环包括用于对每对电极进行充电并用于将电解质中的离子吸附在电极上的充电操作模式,以及用于对该电极放电和用于从一对电极解吸离子的放电模式。 控制器被配置为控制系统,第一和第二电化学脱盐装置具有交错的充放电操作模式。 第一和第二电化学脱盐装置之一处于放电模式,并且至少一对电极释放电流,而第一和第二电化学脱盐装置中的另一个处于充电操作模式并且接收释放的电流 从所述第一和第二电化学脱盐装置中的一个。