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公开(公告)号:US10329160B2
公开(公告)日:2019-06-25
申请号:US15791092
申请日:2017-10-23
Applicant: Malvi Technologies, LLC
Inventor: Vinod Malhotra
IPC: C01D15/00 , C01D15/02 , B01J47/016 , B01J49/60 , B01J41/05 , B01J4/00 , B01J8/00 , B01J41/12 , B01J47/06 , B01J49/07
Abstract: Embodiments of the invention relate to methods and equipment to make lithium hydroxide from lithium salts.
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公开(公告)号:US10221082B2
公开(公告)日:2019-03-05
申请号:US15031555
申请日:2014-10-23
Applicant: LANXESS Sybron Chemicals, Inc.
Inventor: Philip W. Fatula , Anthony P. Tirio , Lillianne Falco , Wilwood Matthews
IPC: C02F1/42 , C01B7/03 , B01J41/14 , B01J41/05 , B01J41/07 , B01J49/07 , B01J49/57 , C02F101/10 , C02F103/10
Abstract: A process for the amelioration of acid mine drainage useful in shale hydrolyic fracturing operations for the production of natural gas involving the exchange of sulfate and chloride ions by an ion exchange resin so as to produce hydrochloric acid and water for use in hydrolyic fracturing operations from acid mine drainage.
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公开(公告)号:US10131552B2
公开(公告)日:2018-11-20
申请号:US14590616
申请日:2015-01-06
Applicant: Amperage Energy Inc.
Inventor: Chad Allen Randal
IPC: C02F1/42 , C02F9/00 , B01J49/07 , C02F101/10 , B01J47/022 , B01J47/012 , C02F101/00 , C02F103/10 , C02F103/36
Abstract: Mobile treatment systems and methods for use in removing sulfates from contaminated water using a pre-treatment subsystem configured to remove particulates and debris from the contaminated water and to produce pre-treated water; a treatment subsystem configured to remove sulfates from the pre-treated water and to produce treated water, the treatment subsystem including at least one treatment tank with a collection unit having one or more filters with pore or inlet sizes of approximately 0.35-1.2 mm; and at least one storage tank configured to collect the treated water. Optionally, the systems and methods may use a backwash subsystem configured to backwash the treatment subsystem.
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公开(公告)号:US20180311619A1
公开(公告)日:2018-11-01
申请号:US15956451
申请日:2018-04-18
Applicant: Amalgamated Research LLC
Inventor: Michael M. Kearney , Timothy E. Pryor
CPC classification number: B01D61/022 , B01D61/027 , B01D61/10 , B01D61/12 , B01D2311/04 , B01D2317/025 , B01J49/07 , B01J49/20 , B01J49/57
Abstract: Methods of regenerating a strong base anion resin are described. The method comprises collecting a salt-containing product from a chromatographic system configured to process a biomass derived material. The salt-containing product is processed through a nanofiltration membrane to collect a salt-containing permeate, which is used to regenerate a spent strong base anion resin. The biomass may be a plant-based material, such as sugar beets or sugar cane. A system for regenerating a strong base anion resin is also described.
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公开(公告)号:US20180105439A1
公开(公告)日:2018-04-19
申请号:US15566652
申请日:2016-04-13
Applicant: Ovivo Inc.
Inventor: Gensbittel Dominique
CPC classification number: C02F1/42 , B01J47/04 , B01J49/07 , B01J49/09 , B01J49/50 , C02F2001/427 , C02F2303/16
Abstract: In an ion-exchange separation system, a single regeneration column provides for separation of anion and cation resins and the regeneration of both cation and anion resins with a very low level of cross-contamination. After regeneration most of the anion layer in the column is withdrawn, and most of the cation layer is withdrawn, but a portion of each layer adjacent to the interface between the layers remains in the column, to isolate these cross-contaminated portions from the regenerated resins. The withdrawn, regenerated anion and cation resins are placed back into the working vessel.
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公开(公告)号:US20250050324A1
公开(公告)日:2025-02-13
申请号:US18928603
申请日:2024-10-28
Inventor: Jordan Poler , James E. Amburgey , Abhispa Sahu , Tim B. Eldred
IPC: B01J41/09 , B01J41/05 , B01J41/07 , B01J41/10 , B01J47/016 , B01J49/07 , B01J49/57 , C02F1/42 , C02F101/34 , C02F101/36
Abstract: In one aspect, separation media are described herein operable for removing one or more water contaminants, including NOM, fluorinated chemicals, and/or derivatives thereof. Briefly, a separation medium comprises a silica-containing granular support; and an oligomeric stationary phase forming a film on individual grains of the granular support. In some embodiments, the oligomeric stationary phase comprises oligomeric chains covalently bound to the individual grains.
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公开(公告)号:US12121046B2
公开(公告)日:2024-10-22
申请号:US17269683
申请日:2019-05-22
Applicant: WEST INVEST SA
Inventor: Stanislas Baudouin , Eric Reynaud
Abstract: Provided herein are methods, systems, and computer-readable media for controlling a deacidification process for an aqueous fluid circulated through a deacidification column. A first pH value, indicative of a pH of the fluid before circulation through the column, is obtained from a first sensor located at an entry of the column. A second pH value, indicative of a pH of the fluid after circulation through the column, is obtained from a second sensor located at an exit of the column. The second pH value is compared to a target pH value for the fluid to determine a pH difference between the second pH value and the target pH value. Based on the first and second pH values, a deacidification capacity of the column is determined. A fluid flow rate of the fluid through the column is adjusted based on the pH difference and the deacidification capacity.
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公开(公告)号:US11642654B2
公开(公告)日:2023-05-09
申请号:US17197665
申请日:2021-03-10
Applicant: Medtronic, Inc.
Inventor: Christopher M. Hobot , Bryant J. Pudil
IPC: B01J20/34 , A61M1/16 , B01J20/28 , B01J49/57 , B01J49/08 , B01J49/07 , A61L2/00 , B01D15/00 , B01J20/02 , B01J20/06 , C01B25/37 , C01G25/02
CPC classification number: B01J20/3475 , A61L2/0088 , A61M1/168 , A61M1/1696 , B01D15/00 , B01J20/0211 , B01J20/0292 , B01J20/06 , B01J20/28052 , B01J20/3433 , B01J49/07 , B01J49/08 , B01J49/57 , C01B25/372 , C01G25/02 , A61L2202/17 , A61L2202/24 , A61M2205/3324 , A61M2205/3331
Abstract: The invention relates to devices, systems, and methods for conditioning a zirconium oxide sorbent module for use in dialysis after recharging. The devices, systems, and methods can provide for conditioning and recharging of zirconium oxide in a single system, or in separate systems.
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公开(公告)号:US10968153B2
公开(公告)日:2021-04-06
申请号:US16945962
申请日:2020-08-03
Applicant: Eagle US 2 LLC
Inventor: Scott A. Sherwood
IPC: C07C17/20 , B01J49/07 , B01J41/14 , C07C17/275 , C07C19/045 , C07C19/01 , C07C19/075 , C07C17/389 , C07C19/03
Abstract: The present invention provides a method of converting a brominated hydrocarbon to a chlorinated hydrocarbon that involves contacting together the brominated hydrocarbon and a chlorinated ion exchange resin that has a water content of less than or equal to 30 percent by weight, based on the total weight of the chlorinated ion exchange resin and the water. The brominated hydrocarbon includes at least one replaceable bromo group, where each replaceable bromo group is independently covalently bonded to an sp3 hybridized carbon. Contact between the brominated hydrocarbon and the chlorinated ion exchange resin results in replacement of at least one replaceable bromo group of the brominated hydrocarbon with a chloro group, and correspondingly conversion of at least a portion of the brominated hydrocarbon to the chlorinated hydrocarbon.
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公开(公告)号:US10919787B2
公开(公告)日:2021-02-16
申请号:US15774612
申请日:2016-11-08
Applicant: SABIC Global Technologies B.V.
Inventor: Roy Van Lier , Syed Azhar Hashmi , Vadlamani Prasad Rao Chaitanya , Sandeep P. Mohandas , Muhammad Mosleh Al-Subhi , Lee Sangjoo , Hasan Mohammed Rashad Haneef
IPC: C02F1/42 , C02F1/66 , B01J47/02 , B01J49/57 , B01J49/07 , B01J41/05 , B01J47/04 , B01J41/04 , C07C51/42 , B01J41/07 , B01J41/12 , C02F103/36 , C02F103/38 , C02F101/32
Abstract: A method for recovering water from purified terephthalic acid production wastewater includes: producing purified terephthalic acid comprising purified terephthalic acid feedstock and wastewater comprising impurities; separating the purified terephthalic acid feedstock from the wastewater comprising impurities; transferring the wastewater to a tank; adjusting the p H of the wastewater with a basic solution; adjusting the temperature of the wastewater; passing the wastewater to a column; contacting the wastewater with an ion exchange resin to remove the impurities; and recovering the water depleted of impurities.
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