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    Catalytic process for conversion of a petroleum residue using a fixed bed hydrodemetallization catalyst
    1.
    发明授权
    Catalytic process for conversion of a petroleum residue using a fixed bed hydrodemetallization catalyst 失效
    使用固定床加氢脱金属催化剂转化石油残渣的催化方法

    公开(公告)号：US6117306A

    公开(公告)日：2000-09-12

    申请号：US942051

    申请日：1997-10-01

    申请人： Frederic Morel ,  Jean-Luc Duplan ,  Thierry Chapus ,  Alain Billon ,  Stephane Kressmann ,  Gerard Heinrich

    发明人： Frederic Morel ,  Jean-Luc Duplan ,  Thierry Chapus ,  Alain Billon ,  Stephane Kressmann ,  Gerard Heinrich

    IPC分类号： C10G69/04 ,  C10G45/00

    CPC分类号： C10G69/04 ,  Y10S208/95

    摘要： A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydrodemetallization section, the section containing at least one fixed bed hydrodemetallization catalyst. At least a portion of the hydrotreated liquid effluent from step a) is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, a fuel fraction and a heavier liquid fraction of the hydrotreated feed are recovered, and at least a portion of the heavier liquid fraction of the hydrotreated feed is sent to a catalytic cracking section in which it is treated under conditions such that a gaseous fraction, a gasoline fraction, a gas oil fraction and a slurry fraction are produced.

    摘要翻译： 用于转化重质烃馏分的方法包括在加氢脱金属部分中处理烃进料，所述部分含有至少一个固定床加氢脱金属催化剂。 将来自步骤a）的加氢处理的液体流出物的至少一部分送至常压蒸馏区，回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区，从真空蒸馏区回收真空馏分和真空残渣; 将至少一部分真空残渣送至脱沥青部分，从其中回收脱沥青烃馏分和残余沥青; 将脱沥青烃馏分的至少一部分送到加氢处理部分，加氢处理的进料的气体馏分，燃料馏分和较重液体馏分从该加氢处理部分回收，加氢处理的进料的至少一部分较重液体馏分 被送到催化裂化部分，其中在气态馏分，汽油馏分，粗柴油馏分和淤浆馏分产生的条件下进行处理。

    Multi-step catalytic process for conversion of a heavy hydrocarbon fraction
    2.
    发明授权
    Multi-step catalytic process for conversion of a heavy hydrocarbon fraction 失效
    用于转化重质烃馏分的多步催化方法

    公开(公告)号：US6017441A

    公开(公告)日：2000-01-25

    申请号：US942047

    申请日：1997-10-01

    申请人： Frederic Morel ,  Gerard Heinrich ,  Stephane Kressmann ,  Alain Billon ,  Jean-Luc Duplan ,  Thierry Chapus

    发明人： Frederic Morel ,  Gerard Heinrich ,  Stephane Kressmann ,  Alain Billon ,  Jean-Luc Duplan ,  Thierry Chapus

    IPC分类号： C10G67/04 ,  C10G69/04 ,  C10G21/00

    CPC分类号： C10G67/0454 ,  C10G69/04

    摘要： A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydroconversion section in the presence of hydrogen, the section comprising at least one three-phase reactor containing at least one ebullated bed hydroconversion catalyst, operating in liquid and gas riser mode, said reactor comprising at least one means for removing catalyst from said reactor and at least one means for adding fresh catalyst to said reactor. At least a portion of the hydroconverted liquid effluent is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; and at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, an atmospheric distillate and a heavier liquid fraction of the hydrotreated feed are recovered by atmospheric distillation separation, said section comprising at least one three-phase reactor containing at least one ebullated bed hvdroconversion catalyst operating in liquid and gas riser mode, the reactor comprising at least one means for extracting catalyst from the reactor and at least one means for adding fresh catalyst to the reactor.

    摘要翻译： 用于转化重质烃馏分的方法包括在氢的存在下在加氢转化段中处理烃进料，该部分包含至少一个含有至少一个沸腾床加氢转化催化剂的三相反应器，其以液体和气体提升管模式运行， 所述反应器包括至少一种用于从所述反应器除去催化剂的装置和用于将新鲜催化剂加入到所述反应器中的至少一种装置。 将至少一部分加氢转化的液体流出物送入常压蒸馏区，回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区，从真空蒸馏区回收真空蒸馏物和真空残渣; 将至少一部分真空残渣送至脱沥青部分，从其中回收脱沥青烃馏分和残余沥青; 并且至少一部分脱沥青烃切割被送到加氢处理部分，通过常压蒸馏分离回收加氢处理的进料的气体馏分，常压馏出物和较重的液体馏分，所述部分包含至少一个三相 反应器包含至少一种以液体和气体提升管模式运行的沸腾床转化催化剂，该反应器包括至少一种用于从反应器中提取催化剂的装置和至少一种用于向反应器中加入新鲜催化剂的装置。

    Multi-step process for conversion of a petroleum residue
    3.
    发明授权
    Multi-step process for conversion of a petroleum residue 失效
    用于转化石油残渣的多步法

    公开(公告)号：US6007703A

    公开(公告)日：1999-12-28

    申请号：US942901

    申请日：1997-10-01

    申请人： Frederic Morel ,  Stephane Kressmann ,  Jean-Luc Duplan ,  Alain Billon ,  Thierry Chapus ,  Gerard Heinrich

    发明人： Frederic Morel ,  Stephane Kressmann ,  Jean-Luc Duplan ,  Alain Billon ,  Thierry Chapus ,  Gerard Heinrich

    IPC分类号： C10G67/04 ,  C10G69/04 ,  C10G45/00

    CPC分类号： C10G69/04 ,  C10G67/0454

    摘要： A process for converting a heavy hydrocarbon fraction comprises treating the hydrocarbon feed in a hydrodemetallization section, the section comprising at least one fixed bed hydrodemetallization catalyst. At least a portion of the hydrotreated liquid effluent from step a) is sent to an atmospheric distillation zone from which a distillate and an atmospheric residue are recovered; at least a portion of the atmospheric residue is sent to a vacuum distillation zone from which a vacuum distillate and a vacuum residue are recovered; at least a portion of the vacuum residue is sent to a deasphalting section from which a deasphalted hydrocarbon cut and residual asphalt are recovered; and at least a portion of the deasphalted hydrocarbon cut is sent to a hydrotreatment section from which a gas fraction, a fuel fraction and a heavier liquid fraction of the hydrotreated feed are recovered, said section comprising at least one three-phase reactor containing at least one ebullated bed hydrotreatment catalyst operating in liquid and gas riser mode, the reactor comprising at least one means for removing catalyst from the reactor and at least one means for adding fresh catalyst to the reactor.

    摘要翻译： 用于转化重质烃馏分的方法包括在加氢脱金属部分中处理烃进料，该部分包含至少一个固定床加氢脱金属催化剂。 将来自步骤a）的加氢处理的液体流出物的至少一部分送至常压蒸馏区，回收馏出物和大气残留物; 将至少一部分大气残留物送至减压蒸馏区，从真空蒸馏区回收真空馏分和真空残渣; 将至少一部分真空残渣送至脱沥青部分，从其中回收脱沥青烃馏分和残余沥青; 并且至少一部分脱沥青烃切割被送到加氢处理部分，从该馏分回收加氢处理的进料的气体馏分，燃料馏分和较重的液体馏分，所述部分包含至少一个至少包含一个三相反应器 一种以液体和气体提升管模式运行的沸腾床加氢处理催化剂，该反应器包括至少一种用于从反应器中除去催化剂的装置和至少一种用于向反应器中加入新鲜催化剂的装置。

    Intensive hydrofining of petroleum fractions
    4.
    发明授权
    Intensive hydrofining of petroleum fractions 失效
    石油馏分的加氢精制

    公开(公告)号：US5954950A

    公开(公告)日：1999-09-21

    申请号：US524631

    申请日：1995-09-07

    申请人： Frederic Morel ,  Pierre Trambouze ,  Jean-Paul Euzen ,  Stephane Kressmann

    发明人： Frederic Morel ,  Pierre Trambouze ,  Jean-Paul Euzen ,  Stephane Kressmann

    IPC分类号： C10G49/00 ,  C10G25/00

    CPC分类号： C10G49/002

    摘要： Intensive hydrofining of petroleum fractions wherein an at least partly together with hydrogen circulate in a given direction, in at least one reactor containing at least one fixed bed of a hydrofining catalyst in solid form, is characterized in that the reactor is equipped with at least one inlet pipe for the mixture of the petroleum fraction and hydrogen and at least one outlet pipe for the resultant hydrofined petroleum fraction, and that at least one static mixer is positioned upstream from said outlet of the hydrofined petroleum fraction.

    摘要翻译： 石油馏分的强化加氢精制，其中至少部分与氢在给定方向循环，在至少一个含有至少一个固体床形式的加氢精制催化剂固定床的反应器中，其特征在于反应器配备有至少一种 用于石油馏分和氢气的混合物的入口管和用于所得加氢精制石油馏分的至少一个出口管，并且至少一个静态混合器位于加氢精炼馏分的出口的上游。

    Method and processing equipment for hydrocarbons and for separation of the phases produced by said processing
    9.
    发明申请
    Method and processing equipment for hydrocarbons and for separation of the phases produced by said processing 审中-公开
    用于碳氢化合物的方法和加工设备以及用于分离由所述处理产生的相

    公开(公告)号：US20050075527A1

    公开(公告)日：2005-04-07

    申请号：US10373197

    申请日：2003-02-26

    申请人： Mathieu Pinault ,  Frederic Hoffmann ,  Stephane Kressmann ,  Pierre Porot ,  John Duddy

    发明人： Mathieu Pinault ,  Frederic Hoffmann ,  Stephane Kressmann ,  Pierre Porot ,  John Duddy

    IPC分类号： B01D19/00 ,  C10G49/12 ,  C07C7/00 ,  B01J10/00

    CPC分类号： B01D19/0042 ,  C10G49/12

    摘要： Method for processing hydrocarbons comprising at least two processing chambers and means for separating the liquid and gaseous fractions contained in the polyphasic mixture produced in the first processing chamber, said mixture coming from a zone (700) where a batch of liquid hydrocarbons, a gaseous batch and solid particles come into contact, said method comprising separation of liquid and gaseous phases located in the chamber. Equipment comprising: a) At least a first chamber comprising means inside said chamber for separating gaseous and liquid fractions coming from said zone, b) means for conveying said liquid fraction toward a second chamber, c) a second chamber comprising a second contact zone and means of introducing, into said zone, a gaseous batch and a liquid batch comprising at least a portion of the liquid fraction coming from the first chamber.

    摘要翻译： 用于处理包含至少两个处理室的烃的方法和用于分离包含在第一处理室中产生的多相混合物中的液相和气态馏分的装置，所述混合物来自区域（700），其中一批液体烃，气态批料 并且固体颗粒接触，所述方法包括分离位于室中的液相和气相。 一种设备，包括：a）至少一个第一室，包括在所述室内的装置，用于分离来自所述区域的气态和液态馏分; b）用于将所述液体馏分输送到第二室的装置，c）第二室，包括第二接触区和 在所述区域中引入气态批料和包含至少一部分来自第一室的液体馏分的液体批料的装置。