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1.发明授权Vessel for regenerating a catalyst for the production of aromatic compounds or for reforming, with improved oxychlorination 有权用于再生用于生产芳族化合物或重整的催化剂的容器，具有改进的氧氯化公开(公告)号：US06426052B1
公开(公告)日：2002-07-30
申请号：US09627075
申请日：2000-07-27
IPC分类号： B01J3844
摘要： A vessel for regenerating a catalyst for reforming or for aromatic compound production comprising a support, at least one noble metal and chlorine, the catalyst being in the form of a moving bed, said vessel comprising at least one combustion zone (A) provided with at least one conduit (9) for introducing oxygen gas and at least one conduit (5) for evacuating gasses from the combustion step, at least one oxychlorination zone (B) and at least one calcining zone (C) provided with at least one conduit (18) for introducing an oxygen-containing gas, said vessel also comprising at least one conduit (1) for introducing catalyst into the vessel, at least one conduit (3) for introducing catalyst from the combustion zone into the following oxychlorination zone (B), and at least one conduit (21) for evacuating gases from the oxychlorination zone comprising at least one means (20) for introducing least one chlorinating agent and at least one means (19) for introducing water and at least one means (17) for introducing an oxygen containing gas.
摘要翻译： 一种用于再生用于重整或芳族化合物生产的催化剂的容器，包括载体，至少一种贵金属和氯，催化剂为移动床的形式，所述容器包括至少一个燃烧区（A），其设置在 用于引入氧气的至少一个导管（9）和用于从燃烧步骤抽空气体的至少一个导管（5），至少一个氧氯化区（B）和至少一个设置有至少一个导管的煅烧区（C） 18，用于引入含氧气体，所述容器还包括用于将催化剂引入容器的至少一个导管（1），用于将催化剂从燃烧区引入到以下氧氯化区（B）中的至少一个导管（3） ，以及用于从氧氯化区排出气体的至少一个导管（21），包括用于引入最少一个氯化剂的至少一个装置（20）和用于引入水的至少一个装置（19）和至少一个装置 （17），用于引入含氧气体。
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2.发明授权Process and unit for regeneration of a catalyst for the production of aromatic compounds or for reforming 有权用于生产芳香族化合物或重整用催化剂再生的方法和单元公开(公告)号：US06277335B1
公开(公告)日：2001-08-21
申请号：US09503731
申请日：2000-02-15
申请人： Marianne Capelle , Jean-Marie Deves , Frédéric Hoffmann , Michel Thery , François-Xavier Brunet , Emmanuelle Bromet
发明人： Marianne Capelle , Jean-Marie Deves , Frédéric Hoffmann , Michel Thery , François-Xavier Brunet , Emmanuelle Bromet
IPC分类号： B01J3800
摘要： The invention concerns a process and unit for regenerating a catalyst for the production of aromatic compounds, in particular for reforming, the catalyst being in a moving bed, comprising combustion, oxychlorination and calcining steps, in which at least one chlorinating agent, at least one oxygen-containing gas, and water are introduced into the oxychlorination step such that the H2O/HCl molar ratio is 1 to 50, the oxychlorination step being carried out in the presence of an oxychlorination gas containing less than 21% of oxygen and at least 50 ppm by weight of chlorine (based on HCl), and at a temperature of 350-600° C., and in which the combustion step is carried out in at least two combustion zones, each zone being separated from the adjacent zones, and at least one gas charged with oxygen is introduced into each zone, the gases produced being extracted from each zone, and in which the severity of the operating conditions increases in the direction of flow of the catalyst.
摘要翻译： 本发明涉及用于再生催化剂的方法和单元，所述催化剂用于生产芳族化合物，特别是重整催化剂在移动床中，包括燃烧，氧氯化和煅烧步骤，其中至少一种氯化剂，至少一种 将含氧气体和水引入到氧氯化步骤中，使得H 2 O / HCl摩尔比为1至50，氧氯化步骤在含有小于21％氧气和至少50％的氧氯化气体存在下进行 ppm（基于HCl），并且在350-600℃的温度下，并且其中燃烧步骤在至少两个燃烧区域中进行，每个区域与相邻区域分离，并且在 将至少一个带有氧气的气体引入每个区域，所产生的气体从每个区域提取，并且其中操作条件的严重性在催化剂流动方向上增加。
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3.发明授权Reactor for chemical conversion of a feedstock in the presence of a diluent, with heat inputs and feedstock/catalyst cross-circulation 有权在稀释剂存在下进行化学转化的反应器，具有热量输入和原料/催化剂交叉循环公开(公告)号：US07070742B2
公开(公告)日：2006-07-04
申请号：US10432774
申请日：2001-11-07
申请人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffmann
发明人： Eric Lenglet , Nicolas Boudet , Frédéric Hoffmann
CPC分类号： B01J8/0496 , B01J8/003 , B01J8/0035 , B01J8/0438 , B01J8/087 , B01J8/12 , B01J2208/00115 , B01J2208/00707
摘要： A reactor with integrated heat for carrying out a chemical conversion process in the presence of a gaseous diluent supplied through one or more ports at the upper and/or lower ends of a catalytic bed through which a feed moves substantially horizontally, and a process for converting a feed, such as a hydrocarbon feed in the reactor.
摘要翻译： 一种具有集成热量的反应器，用于在存在气态稀释剂的情况下进行化学转化过程，所述气体稀释剂通过一个或多个端口在催化床的上端和/或下端通过基本上水平地移动而进入其中; 进料，如反应器中的烃进料。
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4.发明授权Thin multi-stage catalytic reactor with internal heat exchanger, and use thereof 有权具有内部热交换器的薄型多级催化反应器及其应用公开(公告)号：US06919048B2
公开(公告)日：2005-07-19
申请号：US10084493
申请日：2002-02-28
申请人： Frédéric Hoffmann , Eric Lenglet , Philippe Mege
发明人： Frédéric Hoffmann , Eric Lenglet , Philippe Mege
CPC分类号： B01J8/085 , B01J8/003 , B01J8/004 , B01J8/0426 , B01J8/0496 , B01J8/125 , B01J2208/00168 , B01J2219/185 , B01J2219/1943
摘要： An elongate reaction vessel and process includes at least two stages in the vertical direction in which an endothermic or exothermic catalytic reaction is carried out and comprises: a catalytic reaction zone (12a, 12b) per stage (6, 7); introducing (2) a reaction fluid to a stage adapted for transverse motion of the fluid across the whole vertical extent of the reaction zone; introducing and extracting the catalyst; a heat exchanger (5a) for reaction fluids located inside the vessel between two successive reaction zones; means (6) for transporting reaction fluids from one stage to another preferably connected to the exchanger of the stage under consideration and to the inlet for reaction fluids of the subsequent stage; and means for recovering reaction fluids downstream of the last stage. The temperature variation in each zone and the temperature level are respectively adjusted by the thickness of each zone and by heat exchange.
摘要翻译： 细长的反应容器和方法包括沿垂直方向的至少两个阶段，其中进行吸热或放热的催化反应，并包括：每个阶段（6,7）的催化反应区（12a，12b）; 将反应流体引入（2）适于在反应区的整个垂直范围内流体横向运动的阶段; 引入和提取催化剂; 位于两个连续反应区之间的反应流体的热交换器（5a）; 用于将反应流体从一个阶段转移到另一个阶段的装置（6），优选地连接到所考虑的阶段的交换器和后续阶段的反应流体的入口; 以及用于在最后阶段下游回收反应流体的装置。 每个区域的温度变化和温度水平分别通过每个区域的厚度和通过热交换来调整。
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5.发明授权公开(公告)号：US07976698B2
公开(公告)日：2011-07-12
申请号：US10350339
申请日：2003-01-24
IPC分类号： C10G35/04
CPC分类号： B01J37/18 , B01J23/626 , B01J23/6567 , B01J38/10 , C10G35/06
摘要： Process for catalytic conversion in the presence of hydrogen with regeneration of the catalyst that comprises a stage for reduction of said catalyst by the hydrogen that is obtained from the catalytic conversion stage, whereby this hydrogen is purified in advance of impurities that it contains by running it over adsorbent masses, whereby said adsorbent masses are regenerated by an increase in temperature that is provided by the effluent from the reduction stage of the catalyst. Application to the processes for regenerative reforming or dehydrogenation of paraffins and naphthenes and most generally to any moving-bed process that operates in the presence of hydrogen.
摘要翻译： 在氢存在下催化转化的方法，催化剂再生包括由催化转化阶段获得的氢气还原所述催化剂的步骤，由此氢气通过其运行所含有的杂质而纯化 超过吸附剂质量，由此所述吸附剂质量由通过来自催化剂的还原阶段的流出物提供的温度升高而再生。 应用于链烷烃和环烷烃的再生重整或脱氢方法，最常见的是在氢气存在下运行的任何移动床方法。
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公开(公告)号：US06224762B1
公开(公告)日：2001-05-01
申请号：US09389073
申请日：1999-09-02
IPC分类号： B01D1508
CPC分类号： B01J8/0492 , B01D15/1842 , B01D53/0423 , B01D53/0446 , B01D2215/023 , B01D2257/7027 , B01D2259/402 , B01F5/0601 , B01F15/0264 , B01J8/0453 , C07C7/12 , C07C15/08
摘要： Device (DME) or panel for collecting, distributing, mixing or drawing off several fluids, at least one main fluid and at least two secondary fluids, that comprises at least: means for collecting a main fluid (3, 9), at least two injection and/or draw-off rails (6, 7) that allow the passage of secondary fluids, at least two mixing chambers (11a, 11b) that communicate with injection and/or draw-off rails (6, 7) with orifices or passages (6i, 7i), means (12, 4) for redistributing the fluid that is obtained from said mixing chambers, means (5a, 5b) for separating collecting and redistributing means and draw-off rails (6, 7) are arranged one above the other, and mixing chambers (11a, 11b) are arranged on both sides of the rails and symmetrically relative to the orifices that have an injection function.
摘要翻译： 用于收集，分配，混合或抽出多种流体的装置（DME）或面板，至少一个主流体和至少两个次级流体，至少包括：用于收集主流体（3,9）的装置，至少两个 允许次流体通过的至少两个混合室（11a，11b）的喷射和/或牵引轨道（6,7），所述至少两个混合室（11a，11b）与喷嘴和/或排出轨道（6,7） 通道（6i，7i），用于重新分配从所述混合室获得的流体的装置（12,4），用于分离收集和重新分配装置和抽出轨道（6,7）的装置（5a，5b） 并且混合室（11a，11b）相对于具有注射功能的孔对称地布置在轨道的两侧。
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7.发明授权Process for endothermic conversion of hydrocarbons, its uses, and a unit for carrying out the process 失效碳氢化合物的吸热转化方法及其用途以及进行该方法的单元公开(公告)号：US06875338B2
公开(公告)日：2005-04-05
申请号：US09984372
申请日：2001-10-30
申请人： Eric Lenglet , Frédéric Hoffmann , Nicolas Boudet
发明人： Eric Lenglet , Frédéric Hoffmann , Nicolas Boudet
IPC分类号： C10G31/06 , C07B61/00 , C07C5/32 , C07C5/333 , C07C11/00 , C07C15/107 , C10G35/00 , C10G59/02 , C07C2/54
CPC分类号： C10G35/00 , B01J2219/00006 , C07C5/32 , C07C5/3337 , C07C15/107 , C10G2300/1081 , C10G2300/1088 , C10G2300/1096 , C10G2300/4006 , C10G2300/4081 , C10G2300/807 , C10G2400/30 , Y02P20/124 , Y02P20/131 , Y10S585/911 , Y10S585/912 , C07C11/02
摘要： The invention concerns a process for converting hydrocarbons using at least one globally endothermic chemical reaction, in which a hydrocarbon feed successively traverses at least two reaction zones each containing at least one solid catalyst and comprising between said reaction zones an intermediate step, in a non catalytic zone, for reheating the stream (ST) from the first of the two reaction zones prior to its introduction into said second reaction zone, and in which said reheating is carried out in a heat exchanger, with heat transfer essentially by convection using a thermal fluid TF with a coking sensitivity index CS that is less than that of the stream ST, the difference in temperature ΔT between the temperature of the fluid TF at the inlet to the exchanger and the temperature of the stream ST at the heat exchanger outlet being less than 250° C. The invention also concerns the use of said process for converting hydrocarbons and a unit for carrying out the process.
摘要翻译： 本发明涉及使用至少一个全球吸热化学反应转化烃的方法，其中烃类进料依次穿过至少两个含有至少一种固体催化剂的反应区，并且在所述反应区之间包含非催化的中间步骤 区域，用于在其引入所述第二反应区域之前从所述两个反应区域中的第一个重新加热流（ST），并且其中所述再加热在热交换器中进行，其中热传递基本上通过使用热流体的对流 TF具有小于流ST的焦化敏感度指数CS，在交换器入口处的流体TF的温度与热交换器出口处的流ST的温度之间的温差DeltaT小于 本发明还涉及用于转化烃的所述方法和用于进行该方法的单元的使用。
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公开(公告)号：US06454948B2
公开(公告)日：2002-09-24
申请号：US09799015
申请日：2001-03-06
IPC分类号： B01D1508
CPC分类号： B01J8/0492 , B01D15/1842 , B01D53/0423 , B01D53/0446 , B01D2215/023 , B01D2257/7027 , B01D2259/402 , B01F5/0601 , B01F15/0264 , B01J8/0453 , C07C7/12 , C07C15/08
摘要： Device (DME) or panel for collecting, distributing, mixing or drawing off several fluids, at least one main fluid and at least two secondary fluids, that comprises at least: means for collecting a main fluid (3, 9), at least two injection and/or draw-off rails (6, 7) that allow the passage of secondary fluids, at least two mixing chambers (11, 11b) that communicate with injection and/or draw-off rails (6, 7) with orifices or passages (6i, 7i), means (12, 4) for redistributing the fluid that is obtained from said mixing chambers, means (5a, 5b) for separating collecting and redistributing means and draw-off rails (6, 7) are arranged one above the other, and mixing chambers (11a, 11b) are arranged on both sides of the rails and symmetrically relative to the orifices that have an injection function.
摘要翻译： 用于收集，分配，混合或抽出多种流体的装置（DME）或面板，至少一个主流体和至少两个次级流体，至少包括：用于收集主流体（3,9）的装置，至少两个 允许二次流体通过的至少两个混合室（11,11b）的喷射和/或牵引轨道（6,7），所述至少两个混合室（11,11b）与喷嘴和/或排出轨道（6,7） 通道（6i，7i），用于重新分配从所述混合室获得的流体的装置（12,4），用于分离收集和重新分配装置和抽出轨道（6,7）的装置（5a，5b） 并且混合室（11a，11b）相对于具有注射功能的孔对称地布置在轨道的两侧。
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9.发明授权Process for liquid-phase conversion with a moving-bed catalyst using a stripper-lift 失效使用汽提器的移动床催化剂进行液相转化的方法公开(公告)号：US06284939B1
公开(公告)日：2001-09-04
申请号：US09363817
申请日：1999-07-30
IPC分类号： C07C602
CPC分类号： C07C6/04 , B01J8/082 , B01J8/12 , B01J8/1863 , B01J8/20 , B01J38/04 , B01J2219/00006 , B01J2219/00033 , Y02P20/584 , Y10S585/921
摘要： This invention pertains to a continuous catalytic process, for example, for the metathesis of olefins that uses a catalyst circulating in a moving bed in at least one reaction zone operating in the liquid phase and in a regenerator, with a lift to transfer the deactivated catalyst emerging from the reaction zone to the regenerator, whereby said process is characterized by the fact that the transfer is accomplished by a gas that does not react with the catalyst and with the stripping off of at least a portion of the organic matter that is adsorbed on the deactivated catalyst.
摘要翻译： 本发明涉及连续催化方法，例如用于使用在液相中和在再生器中运行的至少一个反应区中的移动床中循环的催化剂的烯烃的复分解，其中升动转移失活的催化剂 从反应区向再生器出现，其中所述方法的特征在于转移是通过不与催化剂反应的气体完成的，并且被吸附在至少一部分有机物上 失活的催化剂。
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