Method, Apparatus And System For Concentrating Solutions Using Evaporation
    5.
    发明申请
    Method, Apparatus And System For Concentrating Solutions Using Evaporation 有权
    使用蒸发浓缩溶液的方法,仪器和系统

    公开(公告)号:US20140061958A1

    公开(公告)日:2014-03-06

    申请号:US13984851

    申请日:2012-05-24

    Abstract: The present disclosure is directed at a system, apparatus and method for concentrating a solution. The system includes a humidification device and a solution flow path for flow of a solution to be concentrated to the humidification device. The humidification device includes humidification media to facilitate evaporation of liquid from the solution to be concentrated to gas as the solution to be concentrated passes through the humidification media thereby concentrating the solution. The method includes flowing a solution to be concentrated along a flow path to a humidification device including humidification media, flowing a gas through the humidification media, and flowing the solution to be concentrated through the humidification media. There is evaporation of liquid from the solution to the gas as the solution passes through the humidification media thereby concentrating the solution and producing a humidified gas. The solution to be concentrated may be salt water and the gas may be air.

    Abstract translation: 本公开涉及用于集中解决方案的系统,装置和方法。 该系统包括加湿装置和用于将浓缩到加湿装置的溶液的流动的溶液流动路径。 加湿装置包括加湿介质,以便随着待浓缩的溶液通过加湿介质从而将液体从待浓缩的溶液中蒸发出来,从而浓缩溶液。 该方法包括使待浓缩的溶液沿着流路流动到包括加湿介质的加湿装置,使气体流过加湿介质,并使待浓缩的溶液流过加湿介质。 当溶液通过加湿介质时,液体从溶液蒸发成气体,从而浓缩溶液并产生加湿气体。 待浓缩的溶液可以是盐水,气体可以是空气。

    REVERSE OSMOSIS SYSTEM AND PROCESS FOR CONCENTRATING A SALTWATER

    公开(公告)号:US20240424447A1

    公开(公告)日:2024-12-26

    申请号:US18750956

    申请日:2024-06-21

    Abstract: A reverse osmosis-based method and system for concentrating a saltwater. The system includes at least first and second reverse osmosis units fluidly connected in series. The membrane of the first reverse osmosis unit has at least a 95% rejection rate for sodium chloride, and the membrane of the second reverse osmosis unit has a 30% to 75% rejection rate for sodium chloride. Permeate from the second reverse osmosis unit is recycled to the first reverse osmosis unit for increased water recovery. Temperatures for the saltwater and/or the recycled permeate are controlled using heat exchangers to help ensure the reverse osmosis units' nominal performance.

    CRYSTALLIZATION OF SALTS FROM HIGH PRESSURE REVERSE OSMOSIS CONCENTRATE

    公开(公告)号:US20230065608A1

    公开(公告)日:2023-03-02

    申请号:US17799911

    申请日:2021-03-01

    Abstract: Zero liquid discharge systems, processes, and techniques for treating a saltwater without evaporative crystallization. The saltwater is treated by a fluidic circuit comprising a high-pressure reverse osmosis (“HPRO”) unit configured to operate at a hydraulic pressure of at least 1,500 psi, a cooling crystallizer, and a solids-liquid separator. The saltwater is first concentrated by the HPRO unit to produce an HPRO brine, which is subsequently cooled to a designated crystallization temperature by the cooling crystallizer. The cooling crystallizer crystallizes salt crystals from the cooled HPRO brine and produces a salt-diminished brine. The solids-liquid separator separates the salt-diminished brine from the salt crystals. The salt-diminished brine from the solids-liquid separator is returned to the HPRO unit for further treatment, which allows additional salts to be crystallized from the returned salt-diminished brine.

    CONTROLLED PRODUCED WATER DESALINATION FOR ENHANCED HYDROCARBON RECOVERY

    公开(公告)号:US20210230024A1

    公开(公告)日:2021-07-29

    申请号:US16341776

    申请日:2017-10-26

    Abstract: Processes, systems, and techniques for treating produced water drawn from a subterranean formation. The produced water is provided and contains dissolved solids and magnesium, calcium, and sodium ions. The produced water is desalinated using an electrically-driven membrane separation apparatus that includes alternating anion exchange membranes and cation exchange membranes defining opposing sides of alternating product and concentrate chambers. The desalinating involves flowing the produced water through the product chamber, flowing a second water through the concentrate chamber, and applying an electric potential across the cation and anion exchange membranes as the produced and second waters flow through the product and concentrate chambers, respectively. The product water is consequently produced and has a total dissolved solids content of between 300 mg/L and 8,000 mg/L, a total concentration of calcium ions and magnesium ions less than 100 mg/L, and a sodium adsorption ratio of 20 to 90.

    Modular humidification-dehumidification apparatus for concentrating solutions
    9.
    发明授权
    Modular humidification-dehumidification apparatus for concentrating solutions 有权
    用于浓缩溶液的模块式加湿除湿装置

    公开(公告)号:US09259667B2

    公开(公告)日:2016-02-16

    申请号:US14384007

    申请日:2013-04-18

    Abstract: A modular humidification-dehumidification (HDH) apparatus and system for concentrating a solution including a plurality of internal modules coupled to each other. The plurality of internal modules includes a humidification module and a dehumidification module in gas flow communication with the humidification module. The humidification module includes humidification media facilitating evaporation of liquid from the solution to gas as the solution passes through the humidification media thereby producing a concentrated solution and a humidified gas. The dehumidification module includes a condensing heat exchanger for condensing vapor from the humidified gas.

    Abstract translation: 一种用于集中包括彼此耦合的多个内部模块的解决方案的模块化加湿除湿(HDH)装置和系统。 多个内部模块包括加湿模块和与加湿模块气体流动连通的除湿模块。 加湿模块包括加湿介质,用于当溶液通过加湿介质时促进液体从溶液中蒸发,从而产生浓缩溶液和加湿气体。 除湿模块包括用于冷凝来自加湿气体的蒸气的冷凝热交换器。

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