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    Apparatus for Heating Regeneration Gas
    2.
    发明申请
    Apparatus for Heating Regeneration Gas 有权
    加热再生气装置

    公开(公告)号：US20090035191A1

    公开(公告)日：2009-02-05

    申请号：US11832152

    申请日：2007-08-01

    申请人： Keith A. Couch ,  Xin X. Zhu ,  James P. Glavin

    发明人： Keith A. Couch ,  Xin X. Zhu ,  James P. Glavin

    IPC分类号： C10G11/12

    CPC分类号： C10G11/18 ,  C10G11/182

    摘要： Disclosed is an apparatus for combusting dry gas to heat the air fed to an FCC regenerator to increase its temperature and minimize production of undesirable combustion products. Preferably, the dry gas is a selected FCC product gas. Alternatively or additionally, dry gas from an FCC product stream is separated and delivered to an expander to recover power before combustion.

    摘要翻译： 公开了一种用于燃烧干燥气体以加热供给FCC再生器的空气以增加其温度并最小化不期望的燃烧产物的产生的装置。 优选地，干燥气体是选定的FCC产物气体。 或者或另外，来自FCC产物流的干燥气体被分离并输送到膨胀器以在燃烧之前回收功率。

    HEAT SOURCE FOR PYROLYSIS PROCESS
    4.
    发明申请
    HEAT SOURCE FOR PYROLYSIS PROCESS 有权

    公开(公告)号：US20220235282A1

    公开(公告)日：2022-07-28

    申请号：US17643044

    申请日：2021-12-07

    申请人： ExxonMobil Research and Engineering Company

    发明人： Brian M. Weiss ,  Sophie Liu ,  Michael R. Harper, JR. ,  Herbert W. Barry ,  Changmin Chun ,  Barrington S. Goldson ,  Justin R. Johnson ,  Faria Nusrat

    IPC分类号： C10G11/18 ,  C10G11/12

    摘要： Systems and methods are provided for using a reverse flow reactor (or another reactor with flows in opposing directions at different parts of a process cycle) for pyrolysis of hydrocarbons. The systems and methods can include a reactor that includes a combustion catalyst to initiate and/or maintain combustion within the reactor in a controlled manner during the heating and/or regeneration portion(s) of the reaction cycle. A fuel can also be used that has a greater resistance to auto-combustion, such as a fuel that is composed primarily of methane and/or other hydrocarbons. During operation, the temperature in at least an initial portion of the reactor can be maintained at a temperature so that auto-ignition of the auto-combustion resistant fuel injected during the heating step(s) is reduced or minimized. This can allow combustion to be initiated when the auto-combustion resistant fuel comes into contact with the catalyst. Additionally, the amount and positioning of the catalyst within the reactor can be controlled so that combustion of the fuel takes place over a substantially longer period of time than combustion during a conventional reactor heating step. Because the fuel is moving within the reactor during combustion, extending the combustion time results in a substantial expansion of the volume where combustion occurs. Optionally in combination with an improved reaction cycle, this can expand the portion of the reactor that is directly heated by combustion, allowing for an improved temperature distribution within the reactor during the pyrolysis step.

    Heat source for pyrolysis process
    9.
    发明授权
    Heat source for pyrolysis process 有权

    公开(公告)号：US11773335B2

    公开(公告)日：2023-10-03

    申请号：US17643044

    申请日：2021-12-07

    申请人： ExxonMobil Technology and Engineering Company

    发明人： Brian M. Weiss ,  Sophie Liu ,  Michael R. Harper, Jr. ,  Herbert W. Barry ,  Changmin Chun ,  Barrington S. Goldson ,  Justin R. Johnson ,  Faria Nusrat

    IPC分类号： C10G11/12 ,  C10G11/18

    CPC分类号： C10G11/182 ,  C10G11/12 ,  C10G2300/703

    摘要： Systems and methods are provided for using a reverse flow reactor (or another reactor with flows in opposing directions at different parts of a process cycle) for pyrolysis of hydrocarbons. The systems and methods can include a reactor that includes a combustion catalyst to initiate and/or maintain combustion within the reactor in a controlled manner during the heating and/or regeneration portion(s) of the reaction cycle. A fuel can also be used that has a greater resistance to auto-combustion, such as a fuel that is composed primarily of methane and/or other hydrocarbons. During operation, the temperature in at least an initial portion of the reactor can be maintained at a temperature so that auto-ignition of the auto-combustion resistant fuel injected during the heating step(s) is reduced or minimized. This can allow combustion to be initiated when the auto-combustion resistant fuel comes into contact with the catalyst. Additionally, the amount and positioning of the catalyst within the reactor can be controlled so that combustion of the fuel takes place over a substantially longer period of time than combustion during a conventional reactor heating step. Because the fuel is moving within the reactor during combustion, extending the combustion time results in a substantial expansion of the volume where combustion occurs. Optionally in combination with an improved reaction cycle, this can expand the portion of the reactor that is directly heated by combustion, allowing for an improved temperature distribution within the reactor during the pyrolysis step.

    Process for converting heavy petroleum residues to hydrogen and gaseous distillable hydrocarbons
    10.
    发明授权
    Process for converting heavy petroleum residues to hydrogen and gaseous distillable hydrocarbons 失效
    将重质石油残渣转化为氢气和气态可馏分烃的方法

    公开(公告)号：US4609456A

    公开(公告)日：1986-09-02

    申请号：US699540

    申请日：1985-02-08

    申请人： Andre Deschamps ,  Claude Dezael ,  Sigismond Franckowiak

    发明人： Andre Deschamps ,  Claude Dezael ,  Sigismond Franckowiak

    IPC分类号： C10G47/02 ,  B01J23/00 ,  B01J23/02 ,  B01J23/22 ,  B01J23/78 ,  B01J27/00 ,  B01J27/232 ,  C10G11/12 ,  C10G47/04 ,  C10G47/26 ,  B01J23/90 ,  C10J3/46

    CPC分类号： C10G47/26 ,  C10G47/04

    摘要： The invention concerns a process for converting heavy petroleum residues to hydrogen and to gaseous and distillable hydrocarbons, comprising the association of a step of hydropyrolysis (inside tube 3) with a step of catalytic steam-gasification of the formed coke (outside tube 3), characterized in that the hydropyrolysis step is performed in the presence of a solid supporting a carbon gasification catalyst circulating between the hydropyrolysis zone and the coke steam-gasification zone, said steam-gasification being performed in the absence of oxygen.The petroleum residue, hydrogen and steam are introduced respectively through lines 5, 6 and 7.The products are withdrawn through line 10. Heat may be supplied by the radiating tube 4.

    摘要翻译： 本发明涉及将重质石油残余物转化为氢气和气态和可馏出烃的方法，其包括加氢热解步骤（管3内）与成形焦炭（外管3）的催化蒸汽气化步骤的关联， 其特征在于，所述加氢热解步骤在支持在所述加氢热解区和所述焦炭蒸汽 - 气化区之间循环的碳气化催化剂的固体存在下进行，所述蒸汽气化在不存在氧的情况下进行。 石油渣，氢气和蒸汽分别通过管线5,6和7引入。产物通过管线10排出。热量可以由辐射管4供应。