中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

14 records (took 0.016 seconds)

    Fluid catalytic cracking process for cracking multiple feedstocks
    2.
    发明授权
    Fluid catalytic cracking process for cracking multiple feedstocks 有权

    公开(公告)号：US11214741B2

    公开(公告)日：2022-01-04

    申请号：US16801019

    申请日：2020-02-25

    Applicant: UOP LLC

    Inventor： Lev Davydov ,  Robert Mehlberg ,  Matthew R. Wojtowicz ,  Patrick D. Walker ,  Sakthivelan Maadasamy Durai ,  Sathit Kulprathipanja

    IPC: C10G11/18 ,  B01J8/18 ,  B01J8/36

    Abstract: A fluid catalytic cracking (FCC) process for cracking multiple feedstocks in a FCC apparatus comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips is provided. A first feed is injected into the riser from first distributor tips. A second feed is injected into the riser from second distributor tips. The first distributor tips and the second distributor tips are positioned at different radii in the riser. The first feed and the second feed are cracked in the riser in the presence of an FCC catalyst to provide a cracked effluent stream. The first distributor tips and the second distributor tips are located into a region of lower catalyst density and a region of higher catalyst density respectively in the riser.

    FLUID CATALYTIC CRACKING PROCESS FOR CRACKING MULTIPLE FEEDSTOCKS
    3.
    发明申请
    FLUID CATALYTIC CRACKING PROCESS FOR CRACKING MULTIPLE FEEDSTOCKS 有权

    公开(公告)号：US20210261870A1

    公开(公告)日：2021-08-26

    申请号：US16801019

    申请日：2020-02-25

    Applicant: UOP LLC

    Inventor： Lev Davydov ,  Robert Mehlberg ,  Matthew R. Wojtowicz ,  Patrick D. Walker ,  Sakthivelan Maadasamy Durai ,  Sathit Kulprathipanja

    IPC: C10G11/18 ,  B01J8/18 ,  B01J8/36

    Abstract: A fluid catalytic cracking (FCC) process for cracking multiple feedstocks in a FCC apparatus comprising a first set of feed distributors having first distributor tips and a second set of feed distributors having second distributor tips is provided. A first feed is injected into the riser from first distributor tips. A second feed is injected into the riser from second distributor tips. The first distributor tips and the second distributor tips are positioned at different radii in the riser. The first feed and the second feed are cracked in the riser in the presence of an FCC catalyst to provide a cracked effluent stream. The first distributor tips and the second distributor tips are located into a region of lower catalyst density and a region of higher catalyst density respectively in the riser.

    PARTIAL BURN COMBUSTOR REGENERATOR
    6.
    发明申请
    PARTIAL BURN COMBUSTOR REGENERATOR 审中-公开

    公开(公告)号：US20180339290A1

    公开(公告)日：2018-11-29

    申请号：US16052311

    申请日：2018-08-01

    Applicant: UOP LLC

    Inventor： Patrick D. Walker

    IPC: B01J38/32 ,  B01J8/26 ,  B01D53/50 ,  B01D53/86 ,  C10G11/18

    Abstract: A process for combusting coke from catalyst in partial burn mode is disclosed. The regenerator comprises two chambers. The bulk of the combustion is performed in a first chamber. Disengagement of the catalyst from gas is conducted in the second chamber. Heated gas with a low fraction of oxygen fluidizes catalyst in the second chamber.

    APPARATUSES AND METHODS FOR FLUID CATALYTIC CRACKING WITH LIMITED PARTICULATE EMISSIONS
    7.
    发明申请
    APPARATUSES AND METHODS FOR FLUID CATALYTIC CRACKING WITH LIMITED PARTICULATE EMISSIONS 审中-公开
    具有有限颗粒排放的流体催化裂化装置和方法

    公开(公告)号：US20160090538A1

    公开(公告)日：2016-03-31

    申请号：US14499639

    申请日：2014-09-29

    Applicant: UOP LLC

    Inventor： Derek Froehle ,  Patrick D. Walker ,  Andrew R. Novotny ,  Stanley Joseph Frey

    IPC: C10G11/05 ,  C10G3/00 ,  C10G55/06

    CPC classification number: C10G3/49 ,  B01J8/30 ,  B01J8/388 ,  B01J2208/00663 ,  C10G11/18 ,  C10G55/06 ,  Y02P30/20

    Abstract: Methods and apparatuses are provided for cracking a hydrocarbon. The method includes contacting a first hydrocarbon stream with a cracking catalyst in a riser. The cracking catalyst is regenerated in a regenerator to produce a flue gas stream having a particulate concentration, where the flue gas stream is vented. A second stream is contacted with the cracking catalyst in the riser while the first hydrocarbon stream is contacted with the catalyst, where the second stream includes a natural oil. The particulate concentration is a second particulate concentration while the second stream contacts the cracking catalyst, and a first particulate concentration prior to the second stream contacting the cracking catalyst. The first particulate concentration is greater than the second particulate concentration.

    Abstract translation: 提供了开裂烃的方法和装置。 该方法包括使第一烃流与提升管中的裂化催化剂接触。 裂化催化剂在再生器中再生以产生具有颗粒浓度的烟道气流，其中烟道气流被排出。 第二物流与提升管中的裂化催化剂接触，同时第一烃流与催化剂接触，其中第二流包含天然油。 颗粒浓度是第二颗粒浓度，而第二流接触裂化催化剂，第二流接触裂化催化剂之前的第一颗粒浓度。 第一颗粒浓度大于第二颗粒浓度。

    EXTENDED CONTACT TIME RISER
    8.
    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：US20160038899A1

    公开(公告)日：2016-02-11

    申请号：US14919846

    申请日：2015-10-22

    Applicant: UOP LLC

    Inventor： Patrick D. Walker ,  Matthew Lippmann ,  Mark Schnaith

    IPC: B01J8/24 ,  C10G11/18 ,  B01J8/18

    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 about 1133 liters and about 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 about 1.5 msec to about 10 msec and through a second section of the riser at a second velocity of more than about 15 msec. 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 msec and 10 msec.

    Abstract translation: 提升器包括与入口导管和出口导管连通的壳体。 壳体由具有约1133升至约45307升之间的体积的保持室限定。 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约1.5毫秒至约10毫秒的第一速度穿过提升管的第一部分，并以大于约15毫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到1.5毫秒和10毫秒之间。

    EQUIPMENT AND METHOD FOR CONTROLLING EMISSIONS OF MONO-NITROGEN OXIDES (NOX) AND CARBON MONOXIDE (CO) FROM FLUID CATALYTIC CRACKING (FCC) UNITS
    9.
    发明申请
    EQUIPMENT AND METHOD FOR CONTROLLING EMISSIONS OF MONO-NITROGEN OXIDES (NOX) AND CARBON MONOXIDE (CO) FROM FLUID CATALYTIC CRACKING (FCC) UNITS 审中-公开
    用于控制来自流体催化裂化（FCC）单体的单一氧化物（NOX）和一氧化碳（CO）的排放的设备和方法

    公开(公告)号：US20150209728A1

    公开(公告)日：2015-07-30

    申请号：US14168880

    申请日：2014-01-30

    Applicant: UOP LLC

    Inventor： Patrick D. Walker

    IPC: B01D53/86

    CPC classification number: C10G11/182 ,  C10G11/187 ,  C10G2300/405

    Abstract: A process for controlling emissions from a regenerator vessel that is part of a fluid catalytic cracking unit including a reactor, where the process includes setting a predetermined temperature value in a control unit, wherein the predetermined temperature is the desired temperature within the regenerator vessel. The process also preferably includes controlling the actual temperature within the regenerator vessel by using the predetermined temperature value set in the control unit to appropriately increase or decrease the amount of catalyst being recycled within the reactor.

    Abstract translation: 用于控制作为包括反应器的流化催化裂化装置的一部分的再生器容器的排放的方法，其中所述方法包括在控制单元中设定预定温度值，其中所述预定温度是所述再生器容器内的期望温度。 该方法还优选包括通过使用设置在控制单元中的预定温度值来控制再生器容器内的实际温度，以适当地增加或减少在反应器内循环的催化剂的量。

    EXTENDED CONTACT TIME RISER
    10.
    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：US20140357917A1

    公开(公告)日：2014-12-04

    申请号：US13907232

    申请日：2013-05-31

    Applicant: UOP LLC

    Inventor： Patrick D. Walker ,  Matthew Lippmann ,  Mark Schnaith

    IPC: B01J19/00 ,  B01J8/18

    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 about 1133 liters and about 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 about 1.5 m/sec to about 10 m/sec and through a second section of the riser at a second velocity of more than about 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。 壳体由具有约1133升至约45307升之间的体积的保持室限定。 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约1.5m / sec至约10m / sec的第一速度行进通过提升管的第一部分，并以大于约15m的第二速度穿过提升管的第二部分 /秒。 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。

Patent Agency Ranking