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公开(公告)号:US20190010410A1
公开(公告)日:2019-01-10
申请号:US16015469
申请日:2018-06-22
IPC分类号: C10G65/10
摘要: Systems and methods are provided for upgrading a high density cracked feedstock, such as a catalytic slurry oil, by hydroprocessing. The upgrading can further include performing a separation on the effluent from hydroprocessing of the cracked feedstock, such as a distillation (i.e., separation based on boiling point) or a solvent-based separation. The separation on the hydroprocessed effluent can allow for separation of an aromatics-enriched fraction and an aromatics-depleted fraction from the hydroprocessed effluent. The aromatics-enriched fraction and aromatics-depleted fraction can then be separately used and/or separately undergo further processing.
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公开(公告)号:US11118120B2
公开(公告)日:2021-09-14
申请号:US16707667
申请日:2019-12-09
发明人: Stephen H. Brown , Samia Ilias , Randolph J. Smiley , Richard Demmin , Shifang Luo , Brenda A. Raich , Aldrin G. Cuevas , Keith Wilson , Jesse R. McManus , Lei Zhang
摘要: A method of upgrading refining streams with high polynucleararomatic hydrocarbon (PNA) concentrations can include: hydrocracking a PNA feed in the presence of a catalyst and hydrogen at 380° C. to 430° C., 2500 psig or greater, and 0.1 hr−1 to 5 hr−1 liquid hourly space velocity (LSHV), wherein the weight ratio of PNA feed to hydrogen is 30:1 to 10:1, wherein the PNA feed comprises 25 wt % or less of hydrocarbons having a boiling point of 700° F. (371° C.) or less and having an aromatic content of 50 wt % or greater to form a product comprising 50 wt % or greater of the hydrocarbons having a boiling point of 700° F. (371° C.) or less and having an aromatic content of 20 wt % or less.
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公开(公告)号:US20200181509A1
公开(公告)日:2020-06-11
申请号:US16707667
申请日:2019-12-09
发明人: Stephen H. Brown , Samia Ilias , Randolph J. Smiley , Richard Demmin , Shifang Luo , Brenda A. Raich , Aldrin G. Cuevas , Keith Wilson , Jesse R. McManus , Lei Zhang
摘要: A method of upgrading refining streams with high polynucleararomatic hydrocarbon (PNA) concentrations can include: hydrocracking a PNA feed in the presence of a catalyst and hydrogen at 380° C. to 430° C., 2500 psig or greater, and 0.1 hr−1 to 5 hr−1 liquid hourly space velocity (LSHV), wherein the weight ratio of PNA feed to hydrogen is 30:1 to 10:1, wherein the PNA feed comprises 25 wt % or less of hydrocarbons having a boiling point of 700° F. (371° C.) or less and having an aromatic content of 50 wt % or greater to form a product comprising 50 wt % or greater of the hydrocarbons having a boiling point of 700° F. (371° C.) or less and having an aromatic content of 20 wt % or less.
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