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公开(公告)号:US20170066979A1
公开(公告)日:2017-03-09
申请号:US14848917
申请日:2015-09-09
Applicant: Chevron U.S.A. Inc.
Inventor: Guan-Dao Lei , Subhasis Bhattacharya , Axel Brait
IPC: C10G67/16 , C10M101/00 , C10M177/00
CPC classification number: C10G67/16 , C10G53/06 , C10G67/00 , C10G67/0409 , C10G67/0418 , C10G67/0445 , C10G73/06 , C10G2300/1096 , C10G2400/08 , C10M101/00 , C10M177/00
Abstract: A process for heavy base oil production, comprising: a. performing an aromatic extraction of a first hydrocarbon feed to produce an aromatic extract, and a waxy raffinate; b. mixing the aromatic extract with a second hydrocarbon feed to make a mixed feed having greater than 2,000 wt ppm sulfur; c. feeding the mixed feed to a hydroprocessing unit to produce a heavy API Group II base oil having a kinematic viscosity at 70° C. from 22.6 to 100 mm2/s. An integrated refinery process unit for making heavy base oils, comprising: a. an aromatic extraction unit fluidly connected to a solvent dewaxing unit and a hydroprocessing unit; b. a first line from the aromatic extraction unit, that feeds an aromatic extract to a second hydrocarbon feed to make a mixed feed having greater than 2,000 wt ppm sulfur; and c. a connection that feeds the mixed feed to the hydroprocessing unit.
Abstract translation: 一种重质基油生产方法,包括:a。 执行第一烃进料的芳族萃取以产生芳族萃取物,和蜡状提余液; b。 将芳族提取物与第二烃进料混合以制备具有大于2,000重量ppm硫的混合进料; C。 将混合的进料加入加氢处理装置中以产生重的API II组基础油,其运动粘度在70℃为22.6至100mm 2 / s。 一种用于制造重质基础油的综合炼油工艺装置,包括:a。 芳烃提取单元,其流体连接到溶剂脱蜡单元和加氢处理单元; b。 来自芳族萃取单元的第一行,其将芳族萃取物进料到第二烃进料以制备具有大于2,000重量ppm硫的混合进料; 和c。 将混合进料送入加氢处理装置的连接。
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公开(公告)号:US09796936B2
公开(公告)日:2017-10-24
申请号:US14848917
申请日:2015-09-09
Applicant: Chevron U.S.A. Inc.
Inventor: Guan-Dao Lei , Subhasis Bhattacharya , Axel Brait
IPC: C10G67/16 , C10G67/00 , C10G67/04 , C10M101/00 , C10M177/00 , C10G53/06 , C10G73/06 , C10G67/02 , C10M101/02
CPC classification number: C10G67/16 , C10G53/06 , C10G67/00 , C10G67/0409 , C10G67/0418 , C10G67/0445 , C10G73/06 , C10G2300/1096 , C10G2400/08 , C10M101/00 , C10M177/00
Abstract: A process for heavy base oil production, comprising: a. performing an aromatic extraction of a first hydrocarbon feed to produce an aromatic extract, and a waxy raffinate; b. mixing the aromatic extract with a second hydrocarbon feed to make a mixed feed having greater than 2,000 wt ppm sulfur; c. feeding the mixed feed to a hydroprocessing unit to produce a heavy API Group II base oil having a kinematic viscosity at 70° C. from 22.6 to 100 mm2/s. An integrated refinery process unit for making heavy base oils, comprising: a. an aromatic extraction unit fluidly connected to a solvent dewaxing unit and a hydroprocessing unit; b. a first line from the aromatic extraction unit, that feeds an aromatic extract to a second hydrocarbon feed to make a mixed feed having greater than 2,000 wt ppm sulfur; and c. a connection that feeds the mixed feed to the hydroprocessing unit.
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