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    FLUID CATALYTIC CRACKING PROCESS INCLUDING ADSORPTION OF HYDROGEN AND A CATALYST FOR THE PROCESS
    11.
    发明申请
    FLUID CATALYTIC CRACKING PROCESS INCLUDING ADSORPTION OF HYDROGEN AND A CATALYST FOR THE PROCESS 审中-公开
    流体催化裂化过程，包括加氢过程中氢和催化剂的吸附

    公开(公告)号：WO2015094654A1

    公开(公告)日：2015-06-25

    申请号：PCT/US2014/068269

    申请日：2014-12-03

    Applicant: UOP LLC

    Inventor： LIPPMANN, Matthew ,  RIO, Alex A. ,  COUCH, Keith A.

    IPC: C10G11/18 ,  C10G25/00

    CPC classification number: C10G11/18 ,  C10G11/02

    Abstract: A process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) adsorbing hydrogen on the catalyst during cracking; and (c) producing a cracked product, preferably propylene, wherein the catalyst comprises (i) a matrix, (ii) a catalytically active material, and (iii) a hydrogen adsorption material. Another process for catalytic cracking includes the steps of: (a) contacting a hydrocarbon feed with a catalyst at catalytic cracking conditions; (b) contacting the hydrocarbon feed with a hydrogen adsorption material; (c) adsorbing hydrogen on the hydrogen adsorption material during cracking; and (d) producing a cracked product, wherein the catalyst comprises (i) a matrix and (ii) a catalytically active material.

    Abstract translation: 催化裂解方法包括以下步骤：（a）在催化裂化条件下使烃进料与催化剂接触; （b）在裂化过程中在催化剂上吸附氢; 和（c）产生裂化产物，优选丙烯，其中催化剂包含（i）基体，（ii）催化活性材料和（iii）氢吸附材料。 另一种催化裂化方法包括以下步骤：（a）在催化裂化条件下使烃进料与催化剂接触; （b）使烃进料与氢吸附材料接触; （c）在开裂期间在氢吸附材料上吸附氢; 和（d）产生裂化产物，其中所述催化剂包含（i）基质和（ii）催化活性材料。

    HYDROPROCESS FOR A HYDROCARBON STREAM FROM COAL TAR
    12.
    发明申请
    HYDROPROCESS FOR A HYDROCARBON STREAM FROM COAL TAR 审中-公开
    来自煤炭的油气田的水文

    公开(公告)号：WO2015077039A1

    公开(公告)日：2015-05-28

    申请号：PCT/US2014/064306

    申请日：2014-11-06

    Applicant: UOP LLC

    Inventor： BARGER, Paul T. ,  BRICKER, Maureen L. ,  KOCAL, Joseph A. ,  LIPPMANN, Matthew

    IPC: C10G45/20

    CPC classification number: C10G47/18 ,  C10G65/10 ,  C10G65/12 ,  C10G67/02

    Abstract: A coal tar process is described. A coal tar stream is provided, and the coal tar stream is separated to provide a plurality of hydrocarbon streams. At least one of the hydrocarbon streams is hydroprocessed in a fluidized bed hydroprocessing zone with a catalyst to provide a gaseous volatile product and a solid heavy hydrocarbon product absorbed onto the catalyst. The gaseous volatile product is separated from the catalyst. The catalyst is regenerating by separating the absorbed heavy hydrocarbon product from the catalyst. The regenerated catalyst is recycled into the hydroprocessing zone.

    Abstract translation: 描述了煤焦油过程。 提供煤焦油流，分离煤焦油流以提供多个烃流。 至少一个烃流在具有催化剂的流化床加氢处理区中加氢处理，以提供吸附在催化剂上的气态挥发性产物和固体重烃产物。 气态挥发产物与催化剂分离。 催化剂通过将吸收的重质烃产物与催化剂分离而再生。 再生催化剂再循环到加氢处理区。

    PROCESS FOR HYDROTREATING A COAL TAR STREAM
    13.
    发明申请
    PROCESS FOR HYDROTREATING A COAL TAR STREAM 审中-公开
    加氢煤AR AR。。。。。。。。。

    公开(公告)号：WO2015076979A1

    公开(公告)日：2015-05-28

    申请号：PCT/US2014/062317

    申请日：2014-10-27

    Applicant: UOP LLC

    Inventor： BRICKER, Maureen L. ,  BARGER, Paul T. ,  KOCAL, Joseph A. ,  LIPPMANN, Matthew ,  VANDEN BUSSCHE, Kurt M.

    IPC: C10G45/04 ,  C10G45/00

    CPC classification number: C10G45/04 ,  C10G45/02 ,  C10G2400/02 ,  C10G2400/04

    Abstract: A process for hydrotreating a coal tar stream is described. A coal tar stream is provided, and the coal tar stream is fractionated into at least a light naphtha range hydrocarbon stream having a boiling point in the range of 85C (185F) to 137.8C (280F). The light naphtha range hydrocarbon stream is hydrotreated by contacting the light naphtha range hydrocarbon stream with a naphtha hydrotreating catalyst

    Abstract translation: 描述了用于加氢处理煤焦油流的方法。 提供煤焦油流，并将煤焦油流分馏成沸点为85℃（137℃）至137.8℃（280°F）的至少一种轻质石脑油烃流。 通过使轻质石脑油范围烃流与石脑油加氢处理催化剂

    EXTENDED CONTACT TIME RISER
    15.
    发明申请
    EXTENDED CONTACT TIME RISER 审中-公开
    延长联系时间上升

    公开(公告)号：WO2014193612A1

    公开(公告)日：2014-12-04

    申请号：PCT/US2014/036903

    申请日：2014-05-06

    Applicant: UOP LLC

    Inventor： WALKER, Patrick D. ,  LIPPMANN, Matthew ,  SCHNAITH, Mark

    IPC: B01J8/18 ,  B01J8/08 ,  B01J19/24

    CPC classification number: B01J8/24 ,  B01J3/065 ,  B01J8/1872 ,  B01J8/30 ,  B01J8/388 ,  B01J2208/00893 ,  C10G11/18 ,  C10G11/187

    Abstract: A riser includes a housing in communication with a entry conduit and an exit conduit. The housing is defined by a holdup chamber having a volume of between 1133 liters and 45307 liters. The riser is designed to receive a hydrocarbon feed and a catalyst. An apparatus for fluid catalytic cracking includes a riser in fluid communication with a reactor vessel. A hydrocarbon feed stream and a catalyst travel through a first section of the riser at a first velocity of between 1.5 m/sec to 10 m/sec and through a second section of the riser at a second velocity of more than 15 m/sec. A process for fluid catalytic cracking uses a riser with a holdup chamber. A hydrocarbon feed and a catalyst decrease in velocity in the holdup chamber to between 1.5 m/sec and 10 m/sec.

    Abstract translation: 提升器包括与入口导管和出口导管连通的壳体。 外壳由体积在1133升至45307升之间的保持室限定。 提升管被设计成接收烃进料和催化剂。 用于流体催化裂化的装置包括与反应器容器流体连通的提升管。 烃进料流和催化剂以1.5米/秒至10米/秒的第一速度穿过提升管的第一部分，并以超过15m /秒的第二速度穿过提升管的第二部分。 用于流化催化裂化的方法使用具有保持室的提升管。 烃进料和催化剂在保持室中的速度降低至1.5m / sec至10m / sec。

    FCC COUNTER-CURRENT REGENERATOR WITH A REGENERATOR RISER
    16.
    发明申请
    FCC COUNTER-CURRENT REGENERATOR WITH A REGENERATOR RISER 审中-公开

    公开(公告)号：WO2018125367A1

    公开(公告)日：2018-07-05

    申请号：PCT/US2017/056769

    申请日：2017-10-16

    Applicant: UOP LLC

    Inventor： DAVYDOV, Lev ,  SANDACZ, Michael S. ,  PALMAS, Paolo ,  FEI, Zhihao ,  LIPPMANN, Matthew

    IPC: B01J38/34 ,  B01J8/44

    Abstract: A counter-current catalyst regenerator with at least two stages of counter-current contact along with a regenerator riser is proposed. Each stage may comprise a permeable barrier that allows upward passage of oxygen-containing gas and downward passage of coked catalyst into each stage, but inhibits upward movement of catalyst to mitigate back mixing and true counter-current contact and efficient combustion of coke from catalyst. The regenerator riser may provide a passage to transport the catalyst and may serve as a secondary stage for coke combustion to provide the regenerated catalyst.

    FCC COUNTER-CURRENT REGENERATOR WITH A REGENERATOR RISER
    17.
    发明申请
    FCC COUNTER-CURRENT REGENERATOR WITH A REGENERATOR RISER 审中-公开

    公开(公告)号：WO2018125366A1

    公开(公告)日：2018-07-05

    申请号：PCT/US2017/056764

    申请日：2017-10-16

    Applicant: UOP LLC

    Inventor： DAVYDOV, Lev ,  SANDACZ, Michael S. ,  PALMAS, Paolo ,  FEI, Zhihao ,  LIPPMANN, Matthew

    IPC: B01J38/34 ,  B01J8/44

    Abstract: A counter-current catalyst regenerator with at least two stages of counter-current contact along with a regenerator riser is proposed. Each stage may comprise a permeable barrier that allows upward passage of oxygen-containing gas and downward passage of coked catalyst into each stage, but inhibits upward movement of catalyst to mitigate back mixing and true counter-current contact and efficient combustion of coke from catalyst. The regenerator riser may provide a passage to transport the catalyst and may serve as a secondary stage for coke combustion to provide the regenerated catalyst.

    METHODS AND APPARATUSES FOR PROCESSING HYDROCARBONS
    20.
    发明申请
    METHODS AND APPARATUSES FOR PROCESSING HYDROCARBONS 审中-公开
    处理油料的方法和装置

    公开(公告)号：WO2015088617A1

    公开(公告)日：2015-06-18

    申请号：PCT/US2014/056937

    申请日：2014-09-23

    Applicant: UOP LLC

    Inventor： SERBAN, Manuela ,  WERBA, Gregory R. ,  LIPPMANN, Matthew ,  SADLER, Clayton Colin ,  GATTUPALLI, Rajeswar

    IPC: C10G35/00

    CPC classification number: C10G35/00 ,  C10G21/00 ,  C10G61/04 ,  C10G63/08 ,  C10G2400/30

    Abstract: Methods and apparatuses for processing hydrocarbons are provided. In one embodiment, a method for processing hydrocarbons includes fractionating a feed stock to form a C6-C10 naphtha stream and a C11 + hydrocarbon stream. The method reforms the C6-C10 naphtha stream. Further, the method cracks the C11 + hydrocarbon stream to form a stream of C6-C10 hydrocarbons and extracts aromatics from the stream of C6-C10 hydrocarbons to form an extract stream. The method includes combining the C6-C10 naphtha stream and the extract stream containing the aromatics. Also, the method includes processing the C6-C10 naphtha stream and the extract stream in an aromatics complex to form selected aromatic products. Further, the embodiment may include reforming raffinate streams.

    Abstract translation: 提供了处理碳氢化合物的方法和装置。 在一个实施方案中，用于处理烃的方法包括分馏原料以形成C6-C10石脑油流和C11 +烃流。 该方法改造C6-C10石脑油流。 此外，该方法裂解C11 +烃流以形成C6-C10烃流，并从C6-C10烃流中提取芳族化合物以形成提取物流。 该方法包括将C6-C10石脑油流和含有芳族化合物的萃取物流组合。 此外，该方法包括在芳族化合物络合物中加工C6-C10石脑油流和萃取物流以形成选定的芳香族产物。 此外，该实施方案可以包括重整残液流。

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