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    Base oil hydrotreating catalyst and process of use
    1.
    发明授权
    Base oil hydrotreating catalyst and process of use 有权

    公开(公告)号：US11559789B2

    公开(公告)日：2023-01-24

    申请号：US17199282

    申请日：2021-03-11

    申请人： CHEVRON U.S.A. INC.

    发明人： Yihua Zhang ,  Guan-Dao Lei ,  Bi-Zeng Zhan

    IPC分类号： B01J23/44 ,  B01J21/12 ,  C10G45/62 ,  C10M101/02 ,  C10M177/00 ,  B01J35/10 ,  C10N70/00

    摘要： An improved hydrotreating catalyst and process for making a base oil product wherein the catalyst comprises a base extrudate that includes a high nanopore volume amorphous silica alumina (ASA) and a second amorphous silica alumina. The catalyst and process generally involve the use of a base extrudate comprising the high nanopore volume ASA and the second ASA in a catalyst to produce hydrotreated dewaxed base oil products by contacting the catalyst with a hydrocarbon feedstock. The catalyst base extrudate advantageously comprises a first amorphous silica alumina having a pore volume in the 11-20 nm pore diameter range of 0.2 to 1.0 cc/g and a second amorphous silica alumina having a pore volume in the 11-20 nm pore diameter range of 0.02 to 0.2 cc/g, with the base extrudate formed from the amorphous silica alumina and the alumina having a total pore volume in the 2-50 nm pore diameter range of 0.12 to 1.80 cc/g. The catalyst further comprises at least one modifier element from Groups 6 to 10 and Group 14 of the Periodic Table. The catalyst and process provide improved aromatics saturation.

    BASE OIL HYDROTREATING CATALYST AND PROCESS OF USE
    2.
    发明申请
    BASE OIL HYDROTREATING CATALYST AND PROCESS OF USE 有权

    公开(公告)号：US20220288566A1

    公开(公告)日：2022-09-15

    申请号：US17199282

    申请日：2021-03-11

    申请人： CHEVRON U.S.A. INC.

    发明人： Yihua ZHANG ,  Guan-Dao LEI ,  Bi-Zeng ZHAN

    IPC分类号： B01J23/44 ,  B01J21/12 ,  B01J35/10 ,  C10M101/02 ,  C10M177/00 ,  C10G45/62

    摘要： An improved hydrotreating catalyst and process for making a base oil product wherein the catalyst comprises a base extrudate that includes a high nanopore volume amorphous silica alumina (ASA) and a second amorphous silica alumina. The catalyst and process generally involve the use of a base extrudate comprising the high nanopore volume ASA and the second ASA in a catalyst to produce hydrotreated dewaxed base oil products by contacting the catalyst with a hydrocarbon feedstock. The catalyst base extrudate advantageously comprises a first amorphous silica alumina having a pore volume in the 11-20 nm pore diameter range of 0.2 to 1.0 cc/g and a second amorphous silica alumina having a pore volume in the 11-20 nm pore diameter range of 0.02 to 0.2 cc/g, with the base extrudate formed from the amorphous silica alumina and the alumina having a total pore volume in the 2-50 nm pore diameter range of 0.12 to 1.80 cc/g. The catalyst further comprises at least one modifier element from Groups 6 to 10 and Group 14 of the Periodic Table. The catalyst and process provide improved aromatics saturation.

    Method for co-production of aviation fuel and diesel
    3.
    发明申请
    Method for co-production of aviation fuel and diesel 有权

    公开(公告)号：US20210371761A1

    公开(公告)日：2021-12-02

    申请号：US17287693

    申请日：2019-10-23

    申请人： HALDOR TOPSØE A/S

    发明人： Asbjørn Sune ANDERSSON ,  Ole Frej ALKILDE ,  Thi Hong Diep DUONG

    IPC分类号： C10G65/12 ,  C10G47/14 ,  C10G3/00 ,  C10G45/62

    摘要： A process plant and a process for production of a hydrocarbon suitable for use as jet fuel from a feedstock being a renewable feedstock or an oxygenate feedstock, including combining the feedstock with an amount of a liquid diluent, directing it to contact a material catalytically active in hydrodeoxygenation under hydrotreating conditions to provide a hydrodeoxygenated intermediate product, separating the hydrodeoxygenated intermediate product in at least two fractions; a vapor fraction and a liquid fraction, directing at least an amount of the liquid fraction to contact a material catalytically active in isomerization under isomerization conditions to provide an isomerized intermediate product, directing at least an amount of the isomerized intermediate product and a stream comprising sulfur to provide a hydrocracked intermediate product, and fractionating the hydrocracked intermediate product to provide at least a hydrocarbon suitable for use as jet fuel.

    Process for producing benzene from C5-C12 hydrocarbon mixture
    5.
    发明授权
    Process for producing benzene from C5-C12 hydrocarbon mixture 有权

    公开(公告)号：US10793491B2

    公开(公告)日：2020-10-06

    申请号：US15318154

    申请日：2015-06-01

    申请人： SABIC Global Technologies B.V.

    发明人： Dustin Fickel ,  Stephen Hall ,  Kumar Prashant ,  Maikel van Iersel ,  Sonia Farrokhpanah

    IPC分类号： C07C4/06 ,  C10G65/14 ,  C10G65/10 ,  B01J29/44 ,  C10G45/00 ,  C07C4/18 ,  C07C6/12 ,  C10G47/18 ,  C10G45/62 ,  C10G65/18 ,  C07C7/04 ,  B01J29/42

    摘要： A process for producing benzene comprising the steps of:(a) separating a source feedstream comprising C5-C12 hydrocarbons including benzene and alkylbenzenes into a first feedstream comprising a higher proportion of benzene than the source feedstream and a second feedstream comprising a lower proportion of benzene than the source feedstream and subsequently, (b) contacting the first feedstream in the presence of hydrogen with a first hydrocracking catalyst, and (c) contacting the second feedstream with hydrogen under second process conditions to produce a second product stream comprising benzene, wherein i) the second process conditions are suitable for hydrocracking and step (c) involves contacting the second feedstream in the presence of hydrogen with a second hydrocracking catalyst, ii) the second process conditions are suitable for toluene disproportionation and involve contacting the second feedstream with a toluene disproportionation catalyst or iii) the second process conditions are suitable for hydrodealkylation.