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    Use of a Catalyst Comprising a Phosphorous Modified Zeolite in an Alcohol Dehydration Process
    2.
    发明申请
    Use of a Catalyst Comprising a Phosphorous Modified Zeolite in an Alcohol Dehydration Process 有权
    在醇脱水过程中使用包含磷改性沸石的催化剂

    公开(公告)号：US20140243570A1

    公开(公告)日：2014-08-28

    申请号：US14236726

    申请日：2012-07-25

    申请人： Nikolai Nesterenko ,  Delphine Minoux ,  Cindy Adam ,  Jean-Pierre Dath ,  Joseph Lopez ,  Patrick Euzen

    发明人： Nikolai Nesterenko ,  Delphine Minoux ,  Cindy Adam ,  Jean-Pierre Dath ,  Joseph Lopez ,  Patrick Euzen

    IPC分类号： C07C1/24

    CPC分类号： C07C1/24 ,  B01J29/40 ,  B01J29/85 ,  B01J37/10 ,  B01J37/28 ,  C07C2527/14 ,  C07C2529/06 ,  C07C2529/40 ,  Y02P20/52 ,  Y02P30/42 ,  C07C11/04

    摘要： A catalyst can be used to convert an alcohol in a dehydration process into an olefin having the same number of carbon atoms as the alcohol. The catalyst can include a phosphorus modified zeolite made by providing a zeolite with at least one ten member ring in the structure, steaming the zeolite, mixing the zeolite with binders and shaping additives, and shaping the zeolite. An ion-exchange step can be performed, and the shaped catalyst can be steamed. Phosphorus can be introduced on the catalyst at an amount of at least 0.1 wt %, such as by dry impregnation or chemical vapor deposition. A metal can be introduced. The catalyst can be washed and/or calcinated, and steamed in an equilibration step. The steaming severity (X) can be at least about 2. The catalyst can be steamed at a temperature above 625° C., such as a temperature ranging from 700 to 800° C.

    摘要翻译： 催化剂可用于将脱水过程中的醇转化为具有与醇相同数目的碳原子的烯烃。 催化剂可以包括通过在结构中提供具有至少一个十元环的沸石而制成的磷改性沸石，蒸煮沸石，将沸石与粘合剂和成型添加剂混合，以及成型沸石。 可以进行离子交换步骤，并且可以蒸成型催化剂。 磷可以以至少0.1重量％的量引入催化剂上，例如通过干浸渍或化学气相沉积。 可以引入金属。 可以将催化剂洗涤和/或煅烧，并在平衡步骤中蒸煮。 蒸汽浓度（X）可以至少约为2.催化剂可以在高于625℃的温度下蒸煮，例如700-800℃的温度。

    Process for the production of phenylalkanes that use a catalyst based on silicated alumina
    6.
    发明授权
    Process for the production of phenylalkanes that use a catalyst based on silicated alumina 有权
    制备使用基于硅酸铝的催化剂的苯基烷烃的方法

    公开(公告)号：US07262333B2

    公开(公告)日：2007-08-28

    申请号：US10981740

    申请日：2004-11-05

    申请人： Patrick Euzen ,  Emmanuelle Guillon

    发明人： Patrick Euzen ,  Emmanuelle Guillon

    IPC分类号： C07C2/68

    CPC分类号： B01J21/12 ,  B01J23/42 ,  B01J35/002 ,  B01J35/1019 ,  B01J35/1038 ,  B01J35/1061 ,  B01J35/108 ,  B01J37/0009 ,  C07C2/66 ,  C07C15/107

    摘要： The invention relates to a process for the production of at least one compound that is selected from among the 2-, 3-, 4-, 5-, and 6-phenylalkanes by alkylation of an aromatic compound by means of at least one olefin that comprises at least 9 carbon atoms per molecule, in the presence of a catalyst that comprises at least one non-zeolitic substrate with a silicated alumina base that contains an amount of more than 6% by weight and less than or equal to 50% by weight of silica (SiO2) and that exhibits particular characteristics, whereby said process is carried out at a temperature of between 30 and 400° C., a pressure of between 0.1 and 10 MPa, an hourly volumetric flow rate of 0.50 to 200 h−1, and an aromatic compound/olefin molar ratio of between 1:1 and 50:1.

    摘要翻译： 本发明涉及一种通过至少一种烯烃将芳族化合物烷基化制备至少一种选自2-，3-，4-，5-和6-苯基烷烃的化合物的方法， 在每个分子中包含至少9个碳原子的催化剂存在下，所述催化剂包含至少一种非沸石基质，其中硅烷氧化铝基质含量超过6重量％且小于或等于50重量％ 的二氧化硅（SiO 2），并且其表现出特定的特性，由此所述方法在30至400℃的温度下进行，压力为0.1至10MPa，小时体积流速为0.50至200h -1 ，芳香族化合物/烯烃的摩尔比为1：1〜50：1。

    Method for treating a hydrocarbon feedstock including resin removal
    7.
    发明申请
    Method for treating a hydrocarbon feedstock including resin removal 有权
    用于处理包括树脂去除的烃原料的方法

    公开(公告)号：US20070108102A1

    公开(公告)日：2007-05-17

    申请号：US10584048

    申请日：2004-12-13

    申请人： Christophe Gueret ,  Raphael Huyghe ,  Hugues Dulot ,  Patrick Euzen

    发明人： Christophe Gueret ,  Raphael Huyghe ,  Hugues Dulot ,  Patrick Euzen

    IPC分类号： C10G7/00 ,  B01D3/00

    CPC分类号： C10G21/14 ,  C10G47/00 ,  C10G67/049 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/301 ,  C10G2300/44

    摘要： The invention relates to a process, including removal of resins, for the treatment of a hydrocarbon charge, at least 80% of the compounds of which have a boiling point which is above or equal to 340° C., in which process: the charge is sent to a fractionation stage during which the recovery takes place of at least one heavy fraction and at least one light fraction, at least some of the heavy fraction is sent to an extraction stage during which resins contained in said heavy fraction are extracted, and a purified fraction is recovered, a mixture is made which comprises at least part of the purified fraction which was obtained in the extraction stage and at least one light fraction which was obtained in the fractionation stage, and the mixture thus obtained is sent to a cracking stage. Drawing to be published.

    摘要翻译： 本发明涉及一种方法，包括除去树脂，用于处理烃装料，其中至少80％的化合物具有高于或等于340℃的沸点，其中所述装料 送入分馏阶段，在此阶段，回收发生至少一个重馏分和至少一个轻馏分，至少部分重馏分被送至萃取阶段，在此阶段萃取所述重馏分中所含的树脂，以及 回收纯化的馏分，制备包含在萃取阶段获得的至少一部分纯化级分和在分馏阶段获得的至少一种轻馏分的混合物，将得到的混合物送入裂化 阶段。 绘图出版。

    Combustion catalyst and combustion process using such a catalyst
    9.
    发明授权
    Combustion catalyst and combustion process using such a catalyst 失效
    燃烧催化剂和使用这种催化剂的燃烧过程

    公开(公告)号：US06284210B1

    公开(公告)日：2001-09-04

    申请号：US08857072

    申请日：1997-05-15

    申请人： Patrick Euzen ,  Eric Tocque ,  Stephane Rebours ,  Gil Mabilon

    发明人： Patrick Euzen ,  Eric Tocque ,  Stephane Rebours ,  Gil Mabilon

    IPC分类号： B01J802

    CPC分类号： F23C13/00 ,  B01J23/894

    摘要： A combustion catalyst comprising a monolithic substrate, a porous support based on refractory inorganic oxide and an active phase formed by cerium, iron and at least one metal selected from the group formed by palladium and platinum, the content of porous support being between 100 and 400 g per liter of catalyst; the content of cerium being between 0.3 and 20% by weight with respect to the porous support; the content of iron being between 0.01 and 3.5% of iron by weight with respect to the porous support; and the content of palladium and/or platinum being between 3 and 20 g per liter of catalyst. The catalyst of the invention is used in particular in processes for the catalytic combustion of hydrocarbons, carbon monoxide, hydrogen or mixtures thereof, in processes involving one or more catalytic stages.

    摘要翻译： 一种燃烧催化剂，其包含整体式基体，基于耐火无机氧化物的多孔载体和由铈，铁和选自钯和铂形成的基团中的至少一种金属形成的活性相，多孔载体的含量为100-400 g每升催化剂; 相对于多孔载体，铈的含量为0.3〜20重量％ 铁的含量相对于多孔载体为铁的重量的0.01％至3.5％; 钯和/或铂的含量为3至20克/升催化剂。本发明的催化剂特别用于烃，一氧化碳，氢气或其混合物的催化燃烧方法中，涉及一种 或更多的催化阶段。

    Process for catalytic combustion with staged fuel injection
    10.
    发明授权
    Process for catalytic combustion with staged fuel injection 失效
    分段燃料喷射催化燃烧过程

    公开(公告)号：US5823761A

    公开(公告)日：1998-10-20

    申请号：US783167

    申请日：1997-01-14

    申请人： Patrick Euzen ,  Jean-Herve Le Gal ,  Gerard Martin

    发明人： Patrick Euzen ,  Jean-Herve Le Gal ,  Gerard Martin

    IPC分类号： F23C99/00 ,  B01J23/89 ,  F23C13/00 ,  F23B7/00

    CPC分类号： F23C13/00 ,  B01J23/894

    摘要： Described is a process of catalytic combustion with staged fuel injection that comprises: a first injection of fuel and air, the passage of the air-fuel mixture that is formed into a catalytic zone, and a second fuel injection into the flow of output from said catalytic zone; with said process being characterized in that said catalytic zone comprises at least one catalyst that comprises a monolithic substrate, a porous support based on a refractory inorganic oxide, and an active phase that comprises cerium, iron, and optionally zirconium, as well as at least one metal that is selected from the group that is formed by palladium and platinum; the content of porous support is between 100 and 400 g per liter of catalyst; the cerium content is between 0.3 and 20% by weight relative to the porous support; the zirconium content is between 0 and 20% by weight relative to the porous support; with the iron content being between 0.01 and 3.5% by weight of iron relative to the porous support; and the palladium and/or platinum content is greater than 3 g per liter of catalyst. The process that uses such a catalyst produces improved performance levels by avoiding the fluctuating nature of combustion and the deactivation of the catalyst.

    摘要翻译： 描述了具有分段燃料喷射的催化燃烧过程，其包括：首先注入燃料和空气，形成催化区的空气 - 燃料混合物的通过，以及从所述第一燃料喷射流入到所述 催化区; 所述方法的特征在于所述催化区域包括至少一种包含整体式底物的催化剂，基于耐火无机氧化物的多孔载体和包含铈，铁和任选的锆的活性相，以及至少 一种选自由钯和铂形成的基团的金属; 多孔载体的含量为每升催化剂100至400g; 铈含量相对于多孔载体为0.3〜20重量％ 锆含量相对于多孔载体为0至20重量％; 铁的含量相对于多孔载体为0.01〜3.5重量％ 并且钯和/或铂含量大于3g / l催化剂。 使用这种催化剂的方法通过避免燃烧的波动特性和催化剂的失活而产生改进的性能水平。