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公开(公告)号:US20190016968A1
公开(公告)日:2019-01-17
申请号:US16017004
申请日:2018-06-25
Applicant: ExxonMobil Research and Engineering Company
Inventor: Ivy D. Johnson , Bhupender S. Minhas , Jessica Wittman , Sara L. Yohe , Thomas Bruno
Abstract: Electro-kinetic separation processes for removing solid particles from hydrocracker process streams are provided herein.
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公开(公告)号:US20200299592A1
公开(公告)日:2020-09-24
申请号:US16808716
申请日:2020-03-04
Applicant: ExxonMobil Research and Engineering Company
Inventor: Bhupender S. Minhas , Ivy D. Johnson , Jessica Wittmann , Jessica E. Gil , Magaly C. Barroeta , Jason M. McMullan , Sarah E. Feicht , F. Pierce Hubbard, JR. , Won M. Kim
Abstract: A method includes introducing a crude oil process stream into an electro-kinetic separator (EKS), passing the crude oil process stream through an electric field generated by the EKS, and removing at least a portion of salt and solid particles from the crude oil process stream as the crude oil process stream passes through the electric field. A product stream is discharged from the EKS with reduced salt and solid particle count as compared to the crude oil process stream.
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公开(公告)号:US09968882B2
公开(公告)日:2018-05-15
申请号:US15274382
申请日:2016-09-23
Applicant: ExxonMobil Research and Engineering Company
Inventor: Simon C. Weston , Mobae Afeworki , Bhupender S. Minhas , Ramesh Gupta , Hugo S. Caram , Manoj K. Chaudhury , Hans Thomann , Hilda B. Vroman , Meghan Nines
CPC classification number: B01D53/0462 , B01D53/0423 , B01D53/0446 , B01D53/1475 , B01D2253/108 , B01D2253/204 , B01D2253/25 , B01D2257/504 , B01J20/18 , B01J20/22 , B01J20/226 , B01J20/262 , B01J20/3204 , B01J20/3206 , B01J20/3214 , B01J20/3246 , B01J20/3272 , Y02C10/08
Abstract: A heat transfer fluid can be used as part of a multi-phase adsorption environment to allow for improved separations of gas components using a solid adsorbent. The heat transfer fluid can reduce or minimize the temperature increase of the solid adsorbent that occurs during an adsorption cycle. Reducing or minimizing such a temperature increase can enhance the working capacity for an adsorbent and/or enable the use of adsorbents that are not practical for commercial scale adsorption using conventional adsorption methods. The multi-phase adsorption environment can correspond to a trickle bed environment, a slurry environment, or another convenient environment where at least a partial liquid phase of a heat transfer fluid is present during gas adsorption by a solid adsorbent.
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公开(公告)号:US20220281784A1
公开(公告)日:2022-09-08
申请号:US17634956
申请日:2020-07-02
Applicant: ExxonMobil Research and Engineering Company
Inventor: Bhupender S. Minhas , Jeevan S. Abichandani , Marcus L.H. van Nuland , Wai Kit Cheng , Chong-Jhoo Wang , Robert G. Tinger
Abstract: Selective removal of non-aromatic hydrocarbons from a xylene isomerization process for para-xylene production is accomplished using a membrane unit positioned within a xylene recovery loop. The membrane unit may include a one-stage or multi-stage (e.g., two-stage) membrane system and may be configured to separate a membrane unit product stream from a non-aromatics rich stream, which can be removed from the xylene recovery loop. The membrane unit may have a xylene permeance of about 60 gm/m2/hr/psi and a xylene to non-aromatic permeance ratio of about 15.
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