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公开(公告)号:US09895682B2
公开(公告)日:2018-02-20
申请号:US14560062
申请日:2014-12-04
Applicant: ExxonMobil Research and Engineering Company
Inventor: Stephen J. McCarthy , Rohit Vijay , Brett Loveless
IPC: B01J29/06 , B01J29/40 , B01J35/10 , B01J29/70 , B01J23/06 , C07C1/22 , B01J27/14 , C07C1/20 , C10G3/00 , C10L1/06 , B01J38/02 , B01J38/12 , B01J21/04 , B01J29/90 , B01J37/02
CPC classification number: B01J29/405 , B01J21/04 , B01J23/06 , B01J27/14 , B01J29/061 , B01J29/40 , B01J29/7049 , B01J29/7057 , B01J29/90 , B01J35/10 , B01J35/1014 , B01J35/1019 , B01J35/1023 , B01J35/1038 , B01J35/1042 , B01J35/1057 , B01J35/108 , B01J35/109 , B01J37/0009 , B01J37/0201 , B01J37/28 , B01J38/02 , B01J38/12 , B01J2229/186 , B01J2229/20 , B01J2229/42 , C07C1/20 , C07C1/22 , C07C2523/06 , C07C2529/06 , C07C2529/40 , C07C2529/70 , C10G3/45 , C10G3/49 , C10G3/55 , C10L1/06 , C10L2200/0423 , C10L2200/0469 , C10L2270/023 , Y02P20/584 , Y02P30/20 , Y02P30/42 , C07C11/02 , C07C15/02
Abstract: A catalyst composition comprises a self-bound zeolite and a Group 12 transition metal selected from the group consisting of Zn, Cd, or a combination thereof, the zeolite having a silicon to aluminum ratio of at least about 10, the catalyst composition having a micropore surface area of at least about 340 m2/g, a molar ratio of Group 12 transition metal to aluminum of about 0.1 to about 1.3, and at least one of: (a) a mesoporosity of greater than about 20 m2/g; (b) a diffusivity for 2,2-dimethylbutane of greater than about 1×10−2 sec−1 when measured at a temperature of about 120° C. and a 2,2-dimethylbutane pressure of about 60 torr (about 8 kPa).
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公开(公告)号:US20130165717A1
公开(公告)日:2013-06-27
申请号:US13712540
申请日:2012-12-12
Applicant: ExxonMobil Research and Engineering Company
Inventor: Stephen John McCarthy , Steven S. Lowenthal , David Lee Johnson , Michel Daage , Jiunn-Shyan Liou , Rohit Vijay , Ajit Bhaskar Dandekar
IPC: C10G69/04
Abstract: This invention relates to methods and processes for increasing the production of FCC (Fluid Catalytic Cracking) gasoline products, and optionally distillate products, from refinery feedstocks. In particular, the processes include hydrotreating and further hydroisomerizing a typical FCC range feedstream prior to catalytically cracking the feedstream in the FCC unit. The methods herein result in higher FCC naphtha yields and lower FCC cat bottoms yields thereby significantly increasing the overall FCC gasoline production for a given operating unit and increasing the profit margin of such FCC unit operations.
Abstract translation: 本发明涉及用于从炼油原料中提高FCC(流体催化裂化)汽油产品的生产方法和方法,以及任选的馏出物。 特别地,所述方法包括加氢处理和进一步加氢异构化典型的FCC范围的原料流,然后在FCC装置中对原料流进行催化裂化。 这些方法导致更高的FCC石脑油产率和较低的FCC猫底产量,从而显着增加给定操作单元的总体FCC汽油产量,并提高FCC装置操作的利润率。
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公开(公告)号:US10105690B2
公开(公告)日:2018-10-23
申请号:US14560081
申请日:2014-12-04
Applicant: ExxonMobil Research and Engineering Company
Inventor: Stephen J. McCarthy , Rohit Vijay , Brett Loveless
IPC: B01J29/06 , B01J29/40 , B01J35/10 , B01J29/70 , B01J23/06 , C07C1/22 , B01J27/14 , C07C1/20 , C10G3/00 , C10L1/06 , B01J38/02 , B01J38/12 , B01J21/04 , B01J29/90 , B01J37/02 , B01J37/00
Abstract: A catalyst composition includes a zeolite, a binder, and a Group 12 transition metal selected from the group consisting of Zn, Cd, or a combination thereof, the zeolite having a silicon to aluminum ratio of at least about 10, the catalyst composition comprising about 50 wt % or less of the binder based on a total weight of the catalyst composition, the catalyst composition having a micropore surface area of at least about 340 m2/g, a molar ratio of Group 12 transition metal to aluminum of about 0.1 to about 1.3, and at least one of (a) a mesoporosity of greater than about 20 m2/g; (b) a diffusivity for 2,2-dimethylbutane of greater than about 1×10−2 sec−1 when measured at a temperature of about 120° C. and a 2,2-dimethylbutane pressure of about 60 torr (about 8 kPa).
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公开(公告)号:US10099209B2
公开(公告)日:2018-10-16
申请号:US14560070
申请日:2014-12-04
Applicant: ExxonMobil Research and Engineering Company
Inventor: Stephen J. McCarthy , Rohit Vijay , Brett Loveless
IPC: B01J29/06 , B01J29/40 , B01J35/10 , B01J29/70 , B01J23/06 , C07C1/22 , B01J27/14 , C07C1/20 , C10G3/00 , C10L1/06 , B01J38/02 , B01J38/12 , B01J21/04 , B01J29/90 , B01J37/02 , B01J37/00
Abstract: A catalyst composition comprising a zeolite, an alumina binder, and a Group 12 transition metal selected from Zn and/or Cd, the zeolite having a Si/Al ratio of at least about 10 and a micropore surface area of at least about 340 m2/g, the catalyst composition comprising about 50 wt % or less of the binder, based on a total weight of the catalyst composition, and having a micropore surface area of at least about 290 m2/g, a molar ratio of Group 12 transition metal to aluminum of about 0.1 to about 1.3, and at least one of: a mesoporosity of about 20 m2/g to about 120 m2/g; a diffusivity for 2,2-dimethylbutane of greater than about 1×10−2 sec−1 when measured at a temperature of about 120° C. and a 2,2-dimethylbutane pressure of about 60 torr (8 kPa); and a combined micropore surface area and mesoporosity of at least about 380 m2/g.
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