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公开(公告)号:US20210309540A1
公开(公告)日:2021-10-07
申请号:US17348139
申请日:2021-06-15
发明人: Ngai Yin YIP , Chanhee BOO , Kinnari SHAH , Ian BILLINGE , Robert WINTON , Eliza DACH
摘要: Systems and methods of performing temperature swing solvent extraction (TSSE) descaling of produced water and desalination of high-salinity brines, e.g., those having a total dissolved solids (TDS) greater than about 250,000 ppm are capable of producing descaled water products including less than about 5% weight percent TDS. The brine/produced water feedstreams and combined with a solvent having temperature-dependent water solubility at a temperature TL. Water is extracted from the feedstream into the solvent to form a water-in-solvent extract component and a raffinate component, from which a solid phase can be precipitated as more water is portioned in the solvent and basicity increases. Heating of the water-in-solvent extract component reduces the solubility of the water therein, producing a biphasic mixture of dewatered solvent and descaled water that can be separated. Because these systems and methods do not require a phase change of water, these products are achieved with significantly higher energy efficiencies when compared to evaporation-based thermal methods.
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公开(公告)号:US20220017385A1
公开(公告)日:2022-01-20
申请号:US17346915
申请日:2020-05-18
发明人: Ngai Yin YIP , Chanhee BOO , Kinnari SHAH , Ian BILLINGE , Robert Winton , Eliza DACH
摘要: Systems and methods of performing temperature swing solvent extraction (TSSE) descaling of produced water and desalination of high-salinity brines, e.g., those having a total dissolved solids (TDS) greater than about 250,000 ppm are capable of producing descaled water products including less than about 5% weight percent TDS. The brine/produced water feedstreams and combined with a solvent having temperature-dependent water solubility at a temperature TL. Water is extracted from the feedstream into the solvent to form a water-in-solvent extract component and a raffinate component, from which a solid phase can be precipitated as more water is portioned in the solvent and basicity increases. Heating of the water-in-solvent extract component reduces the solubility of the water therein, producing a biphasic mixture of dewatered solvent and descaled water that can be separated. Because these systems and methods do not require a phase change of water, these products are achieved with significantly higher energy efficiencies when compared to evaporation-based thermal methods.
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公开(公告)号:US20230242418A1
公开(公告)日:2023-08-03
申请号:US18131444
申请日:2023-04-06
发明人: Ngai Yin YIP , Chanhee BOO , Kinnari SHAH , Ian BILLINGE , Robert WINTON , Eliza DACH
CPC分类号: C02F1/265 , C02F1/042 , C02F1/66 , C02F1/444 , C02F2209/02 , C02F2103/10
摘要: Systems and methods of performing temperature swing solvent extraction (TSSE) descaling of produced water and desalination of high-salinity brines, e.g., those having a total dissolved solids (TDS) greater than about 250,000 ppm are capable of producing descaled water products including less than about 5% weight percent TDS. The brine/produced water feedstreams and combined with a solvent having temperature-dependent water solubility at a temperature TL. Water is extracted from the feedstream into the solvent to form a water-in-solvent extract component and a raffinate component, from which a solid phase can be precipitated as more water is portioned in the solvent and basicity increases. Heating of the water-in-solvent extract component reduces the solubility of the water therein, producing a biphasic mixture of dewatered solvent and descaled water that can be separated. Because these systems and methods do not require a phase change of water, these products are achieved with significantly higher energy efficiencies when compared to evaporation-based thermal methods.
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公开(公告)号:US20230174391A9
公开(公告)日:2023-06-08
申请号:US17348139
申请日:2021-06-15
发明人: Ngai Yin YIP , Chanhee BOO , Kinnari SHAH , Ian BILLINGE , Robert WINTON , Eliza DACH
CPC分类号: C02F1/265 , C02F1/042 , C02F1/66 , C02F1/444 , C02F2103/10
摘要: Systems and methods of performing temperature swing solvent extraction (TSSE) descaling of produced water and desalination of high-salinity brines, e.g., those having a total dissolved solids (TDS) greater than about 250,000 ppm are capable of producing descaled water products including less than about 5% weight percent TDS. The brine/produced water feedstreams and combined with a solvent having temperature-dependent water solubility at a temperature TL. Water is extracted from the feedstream into the solvent to form a water-in-solvent extract component and a raffinate component, from which a solid phase can be precipitated as more water is portioned in the solvent and basicity increases. Heating of the water-in-solvent extract component reduces the solubility of the water therein, producing a biphasic mixture of dewatered solvent and descaled water that can be separated. Because these systems and methods do not require a phase change of water, these products are achieved with significantly higher energy efficiencies when compared to evaporation-based thermal methods.
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