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    Modified riser-reactor reforming process
    1.
    发明授权
    Modified riser-reactor reforming process 失效
    改进的提升管反应器重整过程

    公开(公告)号：US5565090A

    公开(公告)日：1996-10-15

    申请号：US345057

    申请日：1994-11-25

    申请人： Christopher D. Gosling ,  Scott Y. Zhang ,  Paula L. Bogdan

    发明人： Christopher D. Gosling ,  Scott Y. Zhang ,  Paula L. Bogdan

    IPC分类号： C10G35/06 ,  C10G35/14 ,  C10G35/10

    CPC分类号： C10G35/06 ,  C10G35/14 ,  Y10S585/955

    摘要： A catalytic reforming process uses a riser reactor with multiple catalyst injection points to obtain high aromatics yields from a naphtha feedstock. Product from the riser reactor typically is discharged into a fluidized-reforming reactor, in which the reforming reaction is completed and catalyst is separated from hydrogen and hydrocarbons. Hydrocarbons from the reactor are separated to recover an aromatized product. Catalyst is regenerated to remove coke and reduced for reuse in the reforming process.

    摘要翻译： 催化重整方法使用具有多个催化剂注入点的提升管反应器以获得来自石脑油原料的高芳族化合物产率。 来自提升管反应器的产物通常被排放到流化重整反应器中，其中重整反应完成并且催化剂与氢气和烃分离。 将来自反应器的烃分离以回收芳构化产物。 再生催化剂以除去焦炭并在重整过程中减少再利用。

    Modified riser-reactor reforming process with prereactor
    2.
    发明授权
    Modified riser-reactor reforming process with prereactor 失效
    改进的提升管反应器重整过程与预反应器

    公开(公告)号：US6036845A

    公开(公告)日：2000-03-14

    申请号：US72444

    申请日：1998-05-04

    申请人： Gregory A. Funk ,  Christopher D. Gosling ,  Paula L. Bogdan

    发明人： Gregory A. Funk ,  Christopher D. Gosling ,  Paula L. Bogdan

    IPC分类号： B01J23/14 ,  B01J23/40 ,  B01J23/96 ,  C10G35/10 ,  C10G35/14 ,  C10G35/04 ,  B01J23/90 ,  C10G35/06

    CPC分类号： B01J23/40 ,  B01J23/14 ,  B01J23/96 ,  C10G35/10 ,  C10G35/14

    摘要： A catalytic reforming process comprises a prereactor which provides an intermediate stream to a riser reactor with multiple catalyst injection points to obtain high aromatics yields from a naphtha feedstock. Product from the riser reactor typically is discharged into a fluidized-bed reforming reactor, in which the reforming reaction is completed and catalyst is separated from hydrogen and hydrocarbons. Hydrocarbons from the reactor are separated to recover an aromatized product. Catalyst is regenerated to remove coke and reduced for reuse in the reforming process.

    摘要翻译： 催化重整方法包括一个预反应器，该预反应器提供具有多个催化剂注入点的提升管反应器的中间物流，以获得来自石脑油原料的高芳族化合物产率。 来自提升管反应器的产物通常被排放到流化床重整反应器中，其中重整反应完成并且催化剂与氢气和烃分离。 将来自反应器的烃分离以回收芳构化产物。 再生催化剂以除去焦炭并在重整过程中减少再利用。

    PROCESS FOR CONVERTING A HYDROCARBON STREAM, AND OPTIONALLY PRODUCING A HYDROCRACKED DISTILLATE
    5.
    发明申请
    PROCESS FOR CONVERTING A HYDROCARBON STREAM, AND OPTIONALLY PRODUCING A HYDROCRACKED DISTILLATE 有权
    转化烃流的方法，并可选择生产水解馏分

    公开(公告)号：US20130240406A1

    公开(公告)日：2013-09-19

    申请号：US13418788

    申请日：2012-03-13

    申请人： Clayton C. Sadler ,  Christopher D. Gosling

    发明人： Clayton C. Sadler ,  Christopher D. Gosling

    IPC分类号： C10G65/10

    CPC分类号： C10G45/58 ,  C10G47/26 ,  C10G65/10 ,  C10G65/12 ,  C10G69/04 ,  C10G2400/02 ,  C10G2400/30

    摘要： One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.

    摘要翻译： 一个示例性实施方案可以是用于转化烃流的方法。 该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括 至少两个环获得经处理的馏出物。

    Process for Preventing Metal Catalyzed Coking
    7.
    发明申请
    Process for Preventing Metal Catalyzed Coking 有权
    防止金属催化焦化工艺

    公开(公告)号：US20100224534A1

    公开(公告)日：2010-09-09

    申请号：US12397647

    申请日：2009-03-04

    申请人： Keith A. Couch ,  Christopher D. Gosling

    发明人： Keith A. Couch ,  Christopher D. Gosling

    IPC分类号： C10G11/00

    CPC分类号： C10G11/18 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/708 ,  C10G2400/20

    摘要： A process and apparatus is disclosed in which a sulfiding agent is added to a catalytic conversion reactor to prevent metal catalyzed coking. The catalytic reactor may be downstream from a first fluid catalytic cracking reactor that provides C10-hydrocarbons as feed to the downstream catalytic reactor.

    摘要翻译： 公开了一种方法和装置，其中将硫化剂加入到催化转化反应器中以防止金属催化焦化。 催化反应器可以在第一流化催化裂化反应器的下游提供作为进料到下游催化反应器的C10烃。

    Combination process for the conversion of a C.sub.2 -C.sub.6 aliphatic hydrocarbon
    9.
    发明授权
    Combination process for the conversion of a C.sub.2 -C.sub.6 aliphatic hydrocarbon 失效
    用于C2-C6脂族烃转化的组合方法

    公开(公告)号：US4861930A

    公开(公告)日：1989-08-29

    申请号：US250288

    申请日：1988-09-28

    申请人： Paul R. Cottrell ,  Thomas R. Fritsch ,  Christopher D. Gosling

    发明人： Paul R. Cottrell ,  Thomas R. Fritsch ,  Christopher D. Gosling

    IPC分类号： C07C2/76 ,  C07C13/00

    CPC分类号： C07C13/00 ,  C07C2/76 ,  C07C2521/04 ,  C07C2523/42 ,  C07C2529/06

    摘要： A combination process for the conversion of C.sub.2 -C.sub.6 aliphatic hydrocarbons into easily transportable hydrocarbons of greater molecular weight. The combination process comprises converting the C.sub.2 -C.sub.6 aliphatic hydrocarbons to aromatic hydrocarbons in a dehydrocyclodimerization reaction zone after which the aromatic is directly hydrogenated in the presence of hydrogen from the dehydrocyclodimerization reaction step to produce large transportable aliphatic hydrocarbons. It is also an aspect of the invention that the hot hydrogenation reaction zone product stream is used to preheat the feed stream to the dehydrocyclodimerization reaction zone.

    摘要翻译： 用于将C 2 -C 6脂族烃转化为更易分子量较容易运输的烃的组合方法。 组合方法包括在脱氢环化二聚化反应区中将C 2 -C 6脂族烃转化为芳香族烃，之后在脱氢环化二聚反应步骤的氢存在下直接氢化芳族化合物，生成大的可运输的脂族烃。 本发明的另一方面是热加氢反应区产物流用于预热进入脱氢环化二聚化反应区的进料流。