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公开(公告)号：US10301551B2
公开(公告)日：2019-05-28
申请号：US15619149
申请日：2017-06-09
Applicant: UOP LLC
Inventor： Elizabeth A. Carter , Saadet Ulas Acikgoz , Nicholas W. Bridge , Christopher D. Gosling , Gavin P. Towler
Abstract: A crude distillation and refining process and apparatus enables modular supply of the crude distillation column. Crude oil may be heated and then separated into only two liquid products in the crude distillation column. The separation between the light and heavy products may be controlled by the overhead product flow rate. Heat is recovered from an overhead stream and a bottoms stream by pre-heating the incoming crude oil stream by heat exchange with overhead stream and the bottoms stream. In an embodiment, a diesel-range distillate fraction may be condensed from an overhead stream in a first heat exchanger and a naphtha-range fraction may be condensed from the gas stream uncondensed by the first heat exchanger in a second heat exchanger.
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Patent Agency Ranking
公开(公告)号：US20180142172A1
公开(公告)日：2018-05-24
申请号：US15872796
申请日：2018-01-16
Applicant: UOP LLC , SAUDI ARAMCO
Inventor： Christopher D. Gosling , Mary Jo Wier , Gautam T. Kalghatgi
CPC classification number: C10L1/04 , C10G59/00 , C10G63/00 , C10G65/00 , C10G69/00 , C10G2300/301 , C10G2300/305 , C10G2300/307 , C10G2300/308 , Y02P30/48
Abstract: GCI fuel compositions and methods of making them are described. The GCI fuel compositions comprises a fuel blend having an initial boiling point in a range of about 26° C. to about 38° C. and a final boiling point in a range of about 193° C. to less than 250° C., a density of about 0.72 kg/l to about 0.8 kg/l at 15° C., a research octane number of about 70 to about 85, and a cetane number of less than about 27, the fuel blend comprising a naphtha stream and a kerosene stream.
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公开(公告)号：US20180002611A1
公开(公告)日：2018-01-04
申请号：US15619149
申请日：2017-06-09
Applicant: UOP LLC
Inventor： Elizabeth A. Carter , Saadet Ulas Acikgoz , Nicholas W. Bridge , Christopher D. Gosling , Gavin P. Towler
CPC classification number: C10G7/00 , C10G67/02 , C10G2300/202 , C10G2300/205
Abstract: A crude distillation and refining process and apparatus enables modular supply of the crude distillation column. Crude oil may be heated and then separated into only two liquid products in the crude distillation column. The separation between the light and heavy products may be controlled by the overhead product flow rate. Heat is recovered from an overhead stream and a bottoms stream by pre-heating the incoming crude oil stream by heat exchange with overhead stream and the bottoms stream. In an embodiment, a diesel-range distillate fraction may be condensed from an overhead stream in a first heat exchanger and a naphtha-range fraction may be condensed from the gas stream uncondensed by the first heat exchanger in a second heat exchanger.
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公开(公告)号：US10260015B2
公开(公告)日：2019-04-16
申请号：US15872796
申请日：2018-01-16
Applicant: UOP LLC , Saudi Arabian Oil Company
Inventor： Christopher D. Gosling , Mary Jo Wier , Gautam T. Kalghatgi
Abstract: GCI fuel compositions and methods of making them are described. The GCI fuel compositions comprises a fuel blend having an initial boiling point in a range of about 26° C. to about 38° C. and a final boiling point in a range of about 193° C. to less than 250° C., a density of about 0.72 kg/l to about 0.8 kg/l at 15° C., a research octane number of about 70 to about 85, and a cetane number of less than about 27, the fuel blend comprising a naphtha stream and a kerosene stream.
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公开(公告)号：US09982204B2
公开(公告)日：2018-05-29
申请号：US14277475
申请日：2014-05-14
Applicant: UOP LLC
Inventor： Christopher D. Gosling , Gavin P. Towler
CPC classification number: C10G69/04 , B01D3/009 , C10G25/03 , C10G50/00 , C10G69/00 , C10G69/06 , C10G69/126 , C10G2300/301 , C10G2400/30
Abstract: One exemplary embodiment can be a process for producing a chemical feedstock. The process can include passing a feed to a hydrotreatment zone, passing an effluent from the hydrotreatment zone to a fractionation zone, passing a stream including one or more C5-C25 hydrocarbons from the fractionation zone to a fluid catalytic cracking zone to obtain an another stream including one or more C6-C10 hydrocarbons, and passing the another stream to an adsorption zone for removing at least one heteroatom compound having a sulfur or a nitrogen atom.
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6.发明申请公开(公告)号：US20140371497A1
公开(公告)日：2014-12-18
申请号：US14277475
申请日：2014-05-14
Applicant: UOP LLC
Inventor： Christopher D. Gosling , Gavin P. Towler
CPC classification number: C10G69/04 , B01D3/009 , C10G25/03 , C10G50/00 , C10G69/00 , C10G69/06 , C10G69/126 , C10G2300/301 , C10G2400/30
Abstract: One exemplary embodiment can be a process for producing a chemical feedstock. The process can include passing a feed to a hydrotreatment zone, passing an effluent from the hydrotreatment zone to a fractionation zone, passing a stream including one or more C5-C25 hydrocarbons from the fractionation zone to a fluid catalytic cracking zone to obtain an another stream including one or more C6-C10 hydrocarbons, and passing the another stream to an adsorption zone for removing at least one heteroatom compound having a sulfur or a nitrogen atom.
Abstract translation: 一个示例性实施方案可以是用于生产化学原料的方法。 该方法可以包括将进料送入加氢处理区，将来自加氢处理区的流出物送入分馏区，将包含一种或多种C 5 -C 25烃的流从分馏区送至流化催化裂化区，得到另一流 包括一种或多种C 6 -C 10烃，并将另一种物流传递到吸附区，以除去至少一种具有硫原子或氮原子的杂原子化合物。
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