-
公开(公告)号:US12040517B2
公开(公告)日:2024-07-16
申请号:US18314247
申请日:2023-05-09
申请人: Rahul S. Nana , Rafael A. Feria
发明人: Rahul S. Nana , Rafael A. Feria
IPC分类号: C25B9/65 , B01D5/00 , B01D53/18 , B01D61/00 , B01D61/36 , B01D61/46 , B01D69/02 , C25B1/04 , H01M8/04 , H01M8/04029 , H01M8/06 , H01M8/22 , H02N11/00
CPC分类号: H01M8/227 , B01D5/006 , B01D53/18 , B01D61/0022 , B01D61/005 , B01D61/364 , B01D61/46 , B01D69/02 , C25B1/04 , C25B9/65 , H01M8/04029 , H01M8/0693 , H02N11/002 , B01D2313/221 , B01D2313/502 , B01D2325/38
摘要: A method and system of generating electrical power or hydrogen from thermal energy is disclosed. The method includes separating, by a selectively permeable membrane, a first saline solution from a second saline solution, receiving, by the first saline solution and/or the second saline solution, thermal energy from a heat source, and mixing the first saline solution and the second saline solution in a controlled manner, capturing at least some salinity-gradient energy as electrical power as the salinity difference between the first saline solution and the second saline solution decreases. The method further includes transferring, by a heat pump, thermal energy from the first saline solution to the second saline solution, causing the salinity difference between the first saline solution and the second saline solution to increase. The method may include a process of membrane distillation, forward osmosis, evaporation, electrodialysis, and/or salt decomposition for further energy efficiency and power generation.
-
公开(公告)号:US20240228334A1
公开(公告)日:2024-07-11
申请号:US18286016
申请日:2022-04-07
申请人: Cranfield University
CPC分类号: C02F1/447 , B01D61/364 , B01D61/366
摘要: A human solid and liquid waste treatment system including method and apparatus for the separation of solid and liquid waste and the further filtration and purification of liquid waste suitable for recycled use. The system comprises a plurality of pre-filtration units provided up-stream of a membrane distillation unit for the energy efficient filtering of waste liquid.
-
公开(公告)号:US12023630B2
公开(公告)日:2024-07-02
申请号:US18046305
申请日:2022-10-13
申请人: VITO NV
发明人: Wouter Van Hecke , Helmut Elslander , Karolien Vanbroekhoven , Helene De Wever , Herman Beckers
CPC分类号: B01D63/16 , B01D61/027 , B01D61/145 , B01D61/147 , B01D61/3621 , C12M29/04 , C12M47/10 , B01D2311/2688 , B01D2315/02 , B01D2315/04 , B01D2319/06 , B01D2325/10
摘要: A method of obtaining a compound may include adding a substrate to a medium in a reactor, and reacting the substrate in the reactor to form the compound. A first stream is separated from the reaction liquid through a first membrane. A second stream is separated from the reaction liquid through a second membrane. The first membrane is a filtration membrane and the second membrane is configured for liquid-gas or liquid-liquid extraction The first membrane and the second membrane are at least partially immersed in the medium and are moved relative to the reactor during the separation steps.
-
公开(公告)号:US12017182B2
公开(公告)日:2024-06-25
申请号:US17507959
申请日:2021-10-22
发明人: Chen Yang , Bingbing Qin , Yufeng Yang , Kai Wang , Xiucai Liu
IPC分类号: B01D15/08 , B01D3/10 , B01D3/12 , B01D9/00 , B01D25/12 , B01D29/00 , B01D36/00 , B01D61/14 , B01D61/18 , B01D61/36 , B01D69/02
CPC分类号: B01D61/18 , B01D3/10 , B01D3/12 , B01D9/005 , B01D9/0068 , B01D15/08 , B01D25/12 , B01D29/00 , B01D36/00 , B01D61/145 , B01D61/147 , B01D61/149 , B01D61/364 , B01D69/02 , B01D2009/0086 , B01D2311/103 , B01D2311/106 , B01D2311/2626 , B01D2311/2642 , B01D2311/2649 , B01D2311/2669 , B01D2317/025 , B01D2325/0283 , B01D2325/20
摘要: The present disclosure provides a system for refining long chain dicarboxylic acid, comprising: a first membrane filtration unit, for a first membrane filtration of a long chain dicarboxylic acid fermentation broth or a treated liquid therefrom; a first decolorization unit, for carrying out a first decolorization treatment to the filtrate obtained after the membrane filtration; a first acidification/crystallization unit, for carrying out a first acidification/crystallization of a filtrate obtained after the membrane filtration to give a solid-liquid mixture; a first separation unit, for a solid-liquid separation of the solid-liquid mixture; a drying unit, for drying the solid separated by the separation unit to give a first solid. By using the refining system according to the present disclosure, the purity of the obtained product is high, and the disadvantages such as poor quality of the product obtained by crystallization from a solvent and environment pollution caused by a solvent can be overcome.
-
公开(公告)号:US20240189775A1
公开(公告)日:2024-06-13
申请号:US18536159
申请日:2023-12-11
申请人: EvCon GmbH
发明人: Markus Wenzel
CPC分类号: B01D61/3641 , B01D61/366 , B01D63/082 , C02F1/447 , B01D2313/221 , B01D2313/54 , B01D2317/025 , C02F2201/007 , C02F2301/08 , C02F2303/10
摘要: This disclosure relates to a multistage distillation system for concentrating a feed liquid, the system including at least one module being assembled by a stack of frame elements, wherein each module includes at least one stage, such that the system includes in total a plurality of stages configured to be flowed through in series by a main feed liquid. Each stage of the plurality of stages is configured to generate steam and feed the steam to a subsequent stage. The first stage of the plurality of stages is configured to heat the main feed liquid and/or to be fed with heated main feed liquid. The system further includes an intermediate cooling device configured to cool the heated main feed liquid before flowing to at least one of the second to last stages of the plurality of serial stages.
-
公开(公告)号:US11992808B2
公开(公告)日:2024-05-28
申请号:US17260661
申请日:2018-07-23
IPC分类号: B01D61/36
CPC分类号: B01D61/364 , B01D61/366 , B01D2313/221 , B01D2317/025
摘要: A membrane distillation module includes a housing having a hot inlet for receiving a hot feed and a hot outlet for expelling the hot feed; a porous membrane located inside the housing and having an outside surface that defines an enclosure, the outside surface being configured to contact the hot feed, wherein the porous membrane is configured to prevent the hot feed from passing from outside the porous membrane to an inside of the enclosure; and a non-porous conduit located inside the enclosure, the non-porous conduit having an inlet for receiving a cold feed and an outlet for expelling the cold feed.
-
公开(公告)号:US20240149221A1
公开(公告)日:2024-05-09
申请号:US18281116
申请日:2022-02-28
IPC分类号: B01D63/10 , B01D53/22 , B01D61/36 , B01D69/02 , B01D69/12 , B01D71/52 , B01D71/56 , B01D71/70 , B01D71/80
CPC分类号: B01D63/103 , B01D53/228 , B01D61/362 , B01D63/1031 , B01D63/107 , B01D69/02 , B01D69/1216 , B01D71/52 , B01D71/56 , B01D71/70 , B01D71/80 , B01D2313/146 , B01D2315/10 , B01D2325/20
摘要: The present invention provides a spiral membrane element suitable for suppressing a decrease in a permeation rate (or a permeation flux) of a permeated fluid from a separation membrane. A spiral membrane element of the present invention includes: a central tube; a membrane leaf that has a separation membrane and a permeation spacer and is wound around the central tube; and a flow passage spacer that is connected to the permeation spacer and is wound around the central tube on a side closer to the central tube than the membrane leaf is. A pressure loss of the flow passage spacer measured by a predetermined test is smaller than a pressure loss of the permeation spacer.
-
公开(公告)号:US11951438B2
公开(公告)日:2024-04-09
申请号:US18146610
申请日:2022-12-27
申请人: NGK Insulators, Ltd.
发明人: Hirofumi Kan , Atsushi Torii , Kazuki Iida
CPC分类号: B01D53/22 , B01D61/36 , B01D63/06 , C01B3/503 , C01B2203/0405
摘要: A liquid fuel synthesis system includes a liquid fuel synthesis portion and a sweep gas supply unit. The liquid fuel synthesis portion is partitioned into a non-permeation side space and a permeation side space by the separation membrane. A temperature of the sweep gas flowing into the permeation side space is higher than at least one of a temperature of the raw material gas flowing into the non-permeation side space and a temperature of a first outflow gas flowing out of the non-permeation side space. A temperature of a second outflow gas flowing out of the permeation side space is higher than at least one of the temperature of the raw material gas flowing into the non-permeation side space and the temperature of the first outflow gas flowing out of the non-permeation side space.
-
公开(公告)号:US11944937B2
公开(公告)日:2024-04-02
申请号:US17285669
申请日:2019-10-02
IPC分类号: B01D61/36 , C02F1/44 , C02F103/08
CPC分类号: B01D61/368 , B01D61/364 , C02F1/447 , B01D2311/1031 , B01D2311/165 , B01D2311/20 , B01D2311/22 , B01D2313/243 , B01D2313/367 , C02F2103/08 , C02F2201/009 , C02F2209/005 , C02F2209/02 , C02F2209/40
摘要: A method for controlling a membrane distillation system includes determining whether there is a day time or a night time at a location of a solar collector system associated with the membrane distillation system; applying a first control mode during the day time to a flow velocity of a feed used by the membrane distillation system; and applying a second control mode, different from the first control scheme, during the night time, to the feed. The first control scheme is a model-free mode.
-
公开(公告)号:US20240091709A1
公开(公告)日:2024-03-21
申请号:US17768018
申请日:2020-10-09
发明人: Tomotaka Hashimoto , Yuki Suga
IPC分类号: B01D61/36
CPC分类号: B01D61/364 , B01D2323/02 , B01D2323/21839 , B01D2325/02833
摘要: This raw-material liquid concentration system is for use in a pharmaceutical product manufacturing process, and employs a membrane-distillation method involving: bringing a raw-material liquid containing a solvent and a solute into contact with cooling water through a membrane-distillation membrane; passing the solvent in the raw-material liquid through the membrane-distillation membrane in the form of vapor; and causing the solvent to move toward the side of the cooling water, wherein the membrane-distillation membrane is a porous membrane that has a water contact angle of at least 90° at the surface thereof, has an average pore diameter of 0.02-0.5 μm, and has a porosity of 60-90%.
-
-
-
-
-
-
-
-
-