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公开(公告)号:US10131551B2
公开(公告)日:2018-11-20
申请号:US15190404
申请日:2016-06-23
Applicant: CONOCOPHILLIPS COMPANY
Inventor: Joel Minier-Matar , Samir Gharfeh , Altaf Hussain , Samer Adham
IPC: C09K8/58 , C02F1/38 , C02F1/28 , C02F1/02 , C02F103/10 , C02F101/30
Abstract: The invention relates to a process for treating an aqueous solution from a subterranean formation of an oil and gas operation. The aqueous solution can be removed from the subterranean formation and treated in a heated centrifugal separator. The heated centrifugal separator can separate the kinetic hydrate inhibitor from the aqueous solution, and then the aqueous solution can be reintroduced into the subterranean formation.
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公开(公告)号:US11014834B2
公开(公告)日:2021-05-25
申请号:US15585920
申请日:2017-05-03
Applicant: ConocoPhillips Company
Inventor: Arnold Janson , Samer Adham , Joel Minier-Matar , Altaf Hussain , Ana M. Santos
IPC: C02F1/44 , B01D61/00 , B01D63/04 , B01D69/08 , C02F103/08
Abstract: The invention relates to a method and apparatus for treatment of produced or process water from hydrocarbon production to reduce the volume of the produced or process water while simultaneously reducing the salinity of a highly saline stream, for example, the brine from a seawater desalination plant. The method includes causing a feed stream comprising produced or process water to flow through the lumen of a hollow fiber osmotic membrane 4 which is immersed in an open channel 2 or tank of flowing draw solution 6 which has high salinity. In this way, water from the feed stream is drawn through the osmotic membrane 4 by an osmotic pressure differential caused by the difference in salinity between the feed stream and the draw solution 6.
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公开(公告)号:US10392271B2
公开(公告)日:2019-08-27
申请号:US15171429
申请日:2016-06-02
Applicant: CONOCOPHILLIPS COMPANY
Inventor: Arnold Janson , Samir Gharfeh , Samer Adham , Zaid Chowdhury , Joel Minier-Matar
IPC: C02F1/44 , C02F1/66 , C02F101/16 , C02F101/10 , B01D61/24 , C02F1/72 , C02F103/36 , C02F11/122 , C02F103/06
Abstract: A method for removing hydrogen sulfide from a liquid stream is described. The method includes contacting the liquid stream including a first amount of hydrogen sulfide with a first side of a porous gas-liquid separation membrane. The hydrogen sulfide moves through the pores of the membrane from the first side to a second, opposite side of the membrane. The method further includes contacting a receiving fluid with the second, opposite side of the porous membrane to receive the hydrogen sulfide. The liquid stream is thus converted to a reduced-sulfide liquid stream having a second amount of hydrogen sulfide that is less than the first amount of hydrogen sulfide. A method for removing ammonia from a liquid stream is also described.
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