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    • 3. 发明申请
    • CONTROLLED PRODUCED WATER DESALINATION FOR ENHANCED HYDROCARBON RECOVERY
    • 受控生产水的脱盐提高了油气回收率
    • WO2018076115A1
    • 2018-05-03
    • PCT/CA2017/051278
    • 2017-10-26
    • SALTWORKS TECHNOLOGIES INC.
    • YIN, XiangchunSPARROW, BenjaminMAN, Malcolm
    • C02F1/469C02F1/46E21B43/40C02F1/42
    • C02F1/4693C02F1/40C02F1/4695C02F2201/4613C02F2209/005C02F2209/10C02F2209/20Y02A20/134
    • 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.
    • 摘要用于处理从地下地层抽取的采出水的方法,系统和技术。 提供的产出水含有溶解的固体和镁离子,钙离子和钠离子。 采用包括交替阴离子交换膜和阳离子交换膜的电驱动膜分离装置使采出水脱盐,所述交替阴离子交换膜和阳离子交换膜限定交替产物和浓缩物室的相对侧。 脱盐包括使产出的水流过产品室,使第二种水流过浓缩物室,并且当产生的和第二种水分别流过产品和浓缩物室时在阳离子和阴离子交换膜上施加电势。 产生的水因此产生并且总溶解固体含量在300mg / L和8,000mg / L之间,钙离子和镁离子的总浓度小于100mg / L,并且钠吸附比率为20至90