公开(公告)号：US11806668B2

公开(公告)日：2023-11-07

申请号：US17644121

申请日：2021-12-14

申请人： Saline Water Conversion Corporation

发明人： Ahmed Saleh Mohammed Alamoudi ,  Mohammed Farooque Ayumantakath ,  Nikolay Voutchkov ,  Seungwon Ihm ,  Christopher Michael Fellows ,  Eslam Alwaznani

IPC分类号： B01D61/02 ,  B01D9/00 ,  C01F5/34 ,  C01F11/46 ,  B01D9/02

CPC分类号： B01D61/026 ,  B01D9/0059 ,  B01D9/02 ,  C01F5/34 ,  C01F11/468 ,  B01D2009/0086

摘要： A system and method for producing minerals from divalent ion-containing brine stream includes rejecting sulfate from a divalent-ion rich reject stream in a first nanofiltration seawater reverse osmosis (NF-SWRO) unit, producing solid calcium sulfate dihydrate and a magnesium-rich brine stream in a first concentration unit, concentrating the magnesium-rich brine stream to a saturation point of sodium chloride in a second concentration unit, producing solid sodium chloride and a supernatant product stream in a first crystallizing unit, produce a concentrated magnesium-rich bittern stream from the supernatant product stream in a third concentration unit, and at least one of producing hydrated magnesium chloride from the concentrated magnesium-rich bittern stream in a second crystallizing unit and producing anhydrous magnesium chloride by prilling the concentrated magnesium-rich bitterns stream under a hydrogen chloride atmosphere in a dry air process unit.

公开(公告)号：US11884567B2

公开(公告)日：2024-01-30

申请号：US17161054

申请日：2021-01-28

申请人： Saline Water Conversion Corporation

发明人： Ahmed Alamoudi ,  Mohammed Ayumantakath ,  Nikolay Voutchkov ,  Seungwon Ihm ,  Eslam Alwaznani

IPC分类号： C02F9/00 ,  B01D61/02 ,  B01D61/58 ,  B01D63/02 ,  C02F1/44 ,  B01D61/00 ,  C02F103/08

CPC分类号： C02F9/00 ,  B01D61/002 ,  B01D61/025 ,  B01D61/026 ,  B01D61/027 ,  B01D61/58 ,  B01D63/02 ,  B01D2311/06 ,  B01D2311/08 ,  B01D2311/14 ,  B01D2317/022 ,  B01D2317/025 ,  C02F1/441 ,  C02F1/442 ,  C02F1/445 ,  C02F2103/08 ,  C02F2209/03

摘要： A system and method for producing very high concentration brine streams from which commercially efficiently obtained minerals may be obtained is produced by a dual membrane brine concentrator system (DTRI Concentrator). The system includes a nano-filtration system which removes divalent ions from the seawater, a brine concentrator such as a hollow fine fiber forward osmosis system which receives and further concentrates the brine rejected from the nano-filtration system, a SWRO system which receives the NF system permeate and removes monovalent ions, and another brine concentrator which further concentrates the brine rejected from SWRO system. Various permeate and reject brine flow may be forwarded through the Dual Membrane Brine Concentrator system, and multiple stages of the system components may be used, to enhance brine concentration and improve system efficiency.

公开(公告)号：US11795071B2

公开(公告)日：2023-10-24

申请号：US17226452

申请日：2021-04-09

申请人： Saline Water Conversion Corporation

发明人： Ahmed Saleh Mohammed Alamoudi ,  Christopher Michael Fellows ,  Mohammed Farooque Ayumantakath ,  Nikolay Voutchkov ,  Sangho Lee ,  Seungwon Ihm

IPC分类号： C02F1/44 ,  B01D61/02 ,  B01D61/08 ,  C02F103/08

CPC分类号： C02F1/442 ,  B01D61/026 ,  B01D61/027 ,  B01D61/08 ,  B01D2311/08 ,  B01D2311/25 ,  B01D2317/022 ,  B01D2317/025 ,  C02F2103/08 ,  C02F2301/046

摘要： A system and method for producing from saline source water a product containing an increased ratio of multi-valent ions to mono-valent ions, which includes multiple nanofiltration units arranged to selectively remove mono-valent ions from the water fed into each nanofiltration stage in the nanofiltration permeate stream while retaining multi-valent ions in the nanofiltration reject stream. The rate at which the increase in the multi-valent ion- to mono-valent ion ratio is obtained may be enhanced by introduction of lower salinity water into the nanofiltration reject between stages, and by recirculating a portion of downstream nanofiltration reject flow into an upstream nanofiltration unit. The enhanced multi-valent ion product is suitable for multiple uses, including irrigation of plants and remineralization of desalinated water. The relative concentrations of the multi-valent ions in the product may be adjusted, for example by selection of nanofiltration membrane technologies which have higher or lower rejection for specific multi-valent ions.

公开(公告)号：US20230182077A1

公开(公告)日：2023-06-15

申请号：US17644121

申请日：2021-12-14

申请人： Saline Water Conversion Corporation

发明人： Ahmed Saleh Mohammed ALAMOUDI ,  Mohammed Farooque Ayumantakath ,  Nikolay Voutchkov ,  Seungwon Ihm

IPC分类号： B01D61/02 ,  C01F5/34 ,  C01F11/46 ,  B01D9/02 ,  B01D9/00

CPC分类号： B01D61/022 ,  C01F5/34 ,  C01F11/468 ,  B01D9/02 ,  B01D9/0059 ,  B01D2009/0086

摘要： A system and method for producing minerals from divalent ion-containing brine stream includes rejecting sulfate from a divalent-ion rich reject stream in a first nanofiltration seawater reverse osmosis (NF-SWRO) unit, producing solid calcium sulfate dihydrate and a magnesium-rich brine stream in a first concentration unit, concentrating the magnesium-rich brine stream to a saturation point of sodium chloride in a second concentration unit, producing solid sodium chloride and a supernatant product stream in a first crystallizing unit, produce a concentrated magnesium-rich bittern stream from the supernatant product stream in a third concentration unit, and at least one of producing hydrated magnesium chloride from the concentrated magnesium-rich bittern stream in a second crystallizing unit and producing anhydrous magnesium chloride by prilling the concentrated magnesium-rich bitterns stream under a hydrogen chloride atmosphere in a dry air process unit.

公开(公告)号：US10947143B2

公开(公告)日：2021-03-16

申请号：US16371816

申请日：2019-04-01

申请人： Saline Water Conversion Corporation

发明人： Ahmed Saleh Mohammed Alamoudi ,  Mohammed Farooque Ayumantakath ,  Nikolay Voutchkov ,  Seungwon Ihm

IPC分类号： B01D61/00 ,  B01D61/02 ,  B01D61/58 ,  B01D63/02 ,  C02F9/00 ,  C02F1/44 ,  C02F103/08

摘要： A system and method for producing very high concentration brine streams from which commercially efficiently obtained minerals may be obtained is produced by a dual membrane brine concentrator system (DTRI Concentrator). The system includes a nano-filtration system which removes divalent ions from the seawater, a brine concentrator such as a hollow fine fiber forward osmosis system which receives and further concentrates the brine rejected from the nano-filtration system, a SWRO system which receives the NF system permeate and removes monovalent ions, and another brine concentrator which further concentrates the brine rejected from SWRO system. Various permeate and reject brine flow may be forwarded through the Dual Membrane Brine Concentrator system, and multiple stages of the system components may be used, to enhance brine concentration and improve system efficiency.