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11. 发明授权

US5770154A Device for testing and for analyzing a petrochemical process 失效
标题翻译：用于测试和分析石化工艺的设备
公开(公告)号：US5770154A
公开(公告)日：1998-06-23
申请号：US578223
申请日：1995-12-26
申请人： Pierre Bigeard , Stephane Kressmann , Christophe Gueret , Pierre Galtier , Julia Magne-Drisch
发明人： Pierre Bigeard , Stephane Kressmann , Christophe Gueret , Pierre Galtier , Julia Magne-Drisch
IPC分类号： B01J8/02 , G01N31/10 , G01N35/00
CPC分类号： B01J8/0285 , G01N31/10 , B01J2208/00415 , B01J2219/00135
摘要： A device for testing the development of processes or chemical reactions in the presence of solid catalysts comprising a reactor of cylindrical shape, of inside diameter D and of length L, such that 50
摘要翻译：在固体催化剂存在下测试方法或化学反应的发展的装置，其包括内径为D且长度为L的圆柱形反应器，使得50

12. 发明申请

US20060118463A1 Integrated SDA and ebullated-bed process 有权
标题翻译：综合SDA和沸腾床过程
公开(公告)号：US20060118463A1
公开(公告)日：2006-06-08
申请号：US11005062
申请日：2004-12-06
申请人： James Colyar , Stephane Kressmann , Christophe Gueret
发明人： James Colyar , Stephane Kressmann , Christophe Gueret
IPC分类号： C10G67/04
CPC分类号： C10G67/00 , C10G67/0463 , C10G67/049 , C10G69/02 , C10G2400/02 , C10G2400/04
摘要： This invention relates to a novel integrated method for economically processing vacuum residue from heavy crude oils. This is accomplished by utilizing a solvent deasphalter (SDA) in the first step of the process with a C3/C4/C5 solvent such that the DAO product can thereafter be processed in a classic fixed-bed hydrotreater or hydrocracker. The SDA feed also includes recycled stripper bottoms containing unconverted residue/asphaltenes from a downstream steam stripper unit. The asphaltenes from the SDA are sent to an ebullated-bed reactor for conversion of the residue and asphaltenes. Residue conversion in the range of 60-80% is achieved and asphaltene conversion is in the range of 50-70%. The overall residue conversion, with the DAO product considered non-residue, is in the range of 80 W %-90 W % and significantly higher than could be achieved without utilizing the present invention.
摘要翻译：本发明涉及一种用于从重质原油经济处理减压渣油的新型综合方法。这是通过在第一步骤中利用溶剂脱沥青（SDA）与C 3 N 3 C 4 C 5 C 5溶剂使得DAO产品此后可以在经典的固定床加氢处理器或加氢裂化器中加工。 SDA进料还包括来自下游蒸汽汽提塔单元的含有未转化的残余物/沥青质的再循环汽提塔底物。来自SDA的沥青质被送入沸腾床反应器以转化残渣和沥青质。实现了60-80％范围内的残渣转化率，沥青质转化率在50-70％的范围内。考虑到非残留物的DAO产物的总残留物转化率在80W％-90W％的范围内，并且显着高于在不利用本发明的情况下可以实现的。

13. 发明申请

US20050006279A1 Method for the valorization of heavy charges by bubbling-bed deasphalting and hydrocracking 审中-公开
标题翻译：通过鼓泡床脱沥青和加氢裂化来提高重质荷重的方法
公开(公告)号：US20050006279A1
公开(公告)日：2005-01-13
申请号：US10831365
申请日：2004-04-26
申请人： Christophe Gueret , Stephane Kressmann , Jan Verstraete
发明人： Christophe Gueret , Stephane Kressmann , Jan Verstraete
IPC分类号： C10G1/00 , C10G55/06 , C10G67/04 , C10G69/04
CPC分类号： C10G69/04 , C10G2300/107
摘要： The invention relates to a method for treating a hydrocarbons charge comprising the following stages, in which: a) the charge is brought into contact with a solvent in order to obtain a deasphalted effluent having a content of asphaltenes below 3000 ppm by weight, b) the deasphalted effluent is cracked in the presence of hydrogen and a hydrocracking catalyst, in a bubbling-bed reactor, so as to convert at least 50 wt. % of the fraction of the deasphalted effluent boiling above 500° C. to compounds having a boiling point below 500° C., c) the effluent from stage b) is fractionated to recover gasolines, kerosene, gas oils and a first residue, and d) at least a portion of this first residue is cracked so as to obtain an effluent comprising gasolines, kerosene, gas oils and a second residue.
摘要翻译：本发明涉及一种用于处理含有以下阶段的烃装料的方法，其中：a）使电荷与溶剂接触，以获得沥青质含量低于3000重量ppm的脱沥青流出物，b）在氢气和加氢裂化催化剂的存在下，在鼓泡床反应器中将脱沥青的流出物裂化，以便将至少50wt。沸点高于500℃的脱沥青流出物的百分比达到沸点低于500℃的化合物，c）将来自阶段b）的流出物分馏以回收汽油，煤油，瓦斯油和第一残渣，以及 d）该第一残留物的至少一部分被裂化，以获得包含汽油，煤油，瓦斯油和第二残余物的流出物。

14. 发明授权

US06132597A Hydrotreating hydrocarbon feeds in an ebullating bed reactor 失效
标题翻译：在沸腾床反应器中加氢处理烃进料
公开(公告)号：US06132597A
公开(公告)日：2000-10-17
申请号：US95008
申请日：1998-06-10
申请人： Virginie Harle , Slavik Kazstelan , Frederic Morel , Stephane Kressmann , Philippe Courty
发明人： Virginie Harle , Slavik Kazstelan , Frederic Morel , Stephane Kressmann , Philippe Courty
IPC分类号： B01J23/88 , B01J21/04 , B01J23/28 , B01J23/85 , B01J23/883 , B01J35/10 , B01J37/00 , C10G45/04 , C10G45/08 , C10G49/04 , C10G45/06 , C10G47/02
CPC分类号： B01J23/883 , B01J21/04 , B01J23/28 , B01J35/1019 , B01J35/1042 , B01J35/1061 , B01J35/108 , B01J37/0009 , C10G2300/107
摘要： The present invention relates to the use of a catalyst comprising an extruded essentially alumina-based support, constituted by a plurality of juxtaposed agglomerates and partially in the form of packs of flakes and partially in the form of needles, and optionally comprising at least one catalytic metal or a compound of a catalytic metal from group VIB, and/or optionally at least one catalytic metal or compound of a catalytic metal from group VIII, in an ebullating bed process and for hydrorefining and hydroconverting hydrocarbon feeds.
摘要翻译：本发明涉及催化剂的用途，该催化剂包括挤出的基本上为氧化铝的载体，其由多个并置的附聚物构成，并且部分为片状包装形式，部分为针状，并任选地包含至少一种催化剂金属或来自组VIB的催化金属的化合物，和/或任选的至少一种催化金属或来自VIII族的催化金属的化合物，在沸腾床方法中，以及用于加氢精制和加氢转化烃进料。

15. 发明授权

US08618017B2 Irregularly shaped non-spherical supported catalyst, and a process for hydroconversion heavy oil fractions 失效
$Irregularly shaped non-spherical supported catalyst, and a process for hydroconversion heavy oil fractions$
标题翻译：不规则形状的非球形载体催化剂，以及加氢转化重油馏分的方法
公开(公告)号：US08618017B2
公开(公告)日：2013-12-31
申请号：US13463255
申请日：2012-05-03
申请人： Stephane Kressmann , Magalie Roy-Auberger , Jean Luc Le Loarer , Denis Guillaume , Jean Francois Chapat
发明人： Stephane Kressmann , Magalie Roy-Auberger , Jean Luc Le Loarer , Denis Guillaume , Jean Francois Chapat
IPC分类号： C10G45/06
CPC分类号： B01J21/04 , B01J23/85 , B01J23/883 , B01J27/19 , B01J35/0026 , B01J35/026 , B01J35/10 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J35/1066 , B01J35/1071 , B01J37/0018 , B01J37/0036 , B01J37/0063 , B01J37/10 , C10G49/04 , C10G49/12 , C10G2300/205 , C10G2300/4018
摘要： A catalyst for hydrotreating and/or hydroconverting heavy metal-containing hydrocarbon feeds, comprises a support in the form of mainly irregular and non-spherical alumina-based agglomerates the specific shape. The catalyst is prepared by a specific order of steps: crushing, calcining, acidic autoclaving, drying, further calcining and impregnation with catalytic metals.
摘要翻译：用于加氢处理和/或加氢转化含重金属的烃进料的催化剂包括主要为不规则和非球形的氧化铝基附聚物形式的支撑体。催化剂通过以下步骤的特定顺序制备：粉碎，煅烧，酸性高压灭菌，干燥，进一步煅烧和用催化金属浸渍。

16. 发明申请

US20120245023A1 IRREGULARLY SHAPED NON-SPHERICAL SUPPORTED CATALYST, AND A PROCESS FOR HYDROCONVERSION HEAVY OIL FRACTIONS 失效
标题翻译：不规则形状的非球形载体催化剂，以及用于加氢重油的方法
公开(公告)号：US20120245023A1
公开(公告)日：2012-09-27
申请号：US13463255
申请日：2012-05-03
申请人： Stephane KRESSMANN , Magalie ROY-AUBERGER , Jean Luc LELOARER , Denis GUILLAUME , Jean Francois CHAPAT
发明人： Stephane KRESSMANN , Magalie ROY-AUBERGER , Jean Luc LELOARER , Denis GUILLAUME , Jean Francois CHAPAT
IPC分类号： B01J37/08 , B01J21/04
CPC分类号： B01J21/04 , B01J23/85 , B01J23/883 , B01J27/19 , B01J35/0026 , B01J35/026 , B01J35/10 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J35/1066 , B01J35/1071 , B01J37/0018 , B01J37/0036 , B01J37/0063 , B01J37/10 , C10G49/04 , C10G49/12 , C10G2300/205 , C10G2300/4018
摘要： A catalyst for hydrotreating and/or hydroconverting heavy metal-containing hydrocarbon feeds, comprises a support in the form of mainly irregular and non-spherical alumina-based agglomerates the specific shape. The catalyst is prepared by a specific order of steps: crushing, calcining, acidic autoclaving, drying, further calcining and impregnation with catalytic metals.
摘要翻译：用于加氢处理和/或加氢转化含重金属的烃进料的催化剂包括主要为不规则和非球形的氧化铝基附聚物形式的支撑体。催化剂通过以下步骤的特定顺序制备：粉碎，煅烧，酸性高压灭菌，干燥，进一步煅烧和用催化金属浸渍。

17. 发明授权

US5954950A Intensive hydrofining of petroleum fractions 失效
$Intensive hydrofining of petroleum fractions$
标题翻译：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。

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