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    SUBCUTANEOUS IMPLANTS RELEASING AN ACTIVE PRINCIPLE OVER AN EXTENDER PERIOD OF TIME
    1.
    发明申请
    SUBCUTANEOUS IMPLANTS RELEASING AN ACTIVE PRINCIPLE OVER AN EXTENDER PERIOD OF TIME 审中-公开
    时间延长的时间段内的繁琐的植入物释放活跃的原理

    公开(公告)号：US20100003298A1

    公开(公告)日：2010-01-07

    申请号：US12309875

    申请日：2007-08-01

    申请人： Patrice Mauriac ,  Pierre Marion

    发明人： Patrice Mauriac ,  Pierre Marion

    IPC分类号： A61F2/00 ,  A61K38/16

    CPC分类号： A61K9/1694 ,  A61K9/0024 ,  A61K9/1647

    摘要： Subcutaneous implants obtained by extrusion containing (1) microparticles 5 containing an active ingredient dispersed in a PLGA matrix, and optionally microparticles (2) consisting of the same active ingredient or (2′) of a different active ingredient preferably belonging to the same category as that contained in (1) all said microparticles (1) being dispersed in a matrix of PLGA (3), having a glass transition temperature lower than that of the PLGA contained in (1).

    摘要翻译： 通过挤出获得的皮下植入物，其含有（1）分散在PLGA基质中的活性成分的微粒5，以及任选的由不同活性成分或（2'）组成的微粒（2），所述活性成分优选属于与 （1）中所含的所有微粒（1）分散在PLGA（3）的基质中，玻璃化转变温度低于（1）中所含的PLGA的玻璃化转变温度。

    Process for converting heavy petroleum fractions including an ebulliated bed for producing middle distillates with a low sulfur content
    2.
    发明授权
    Process for converting heavy petroleum fractions including an ebulliated bed for producing middle distillates with a low sulfur content 有权
    用于转化重质石油馏分的方法，包括用于生产低硫含量的中间馏分的沸腾床

    公开(公告)号：US07390393B2

    公开(公告)日：2008-06-24

    申请号：US11505285

    申请日：2006-08-17

    申请人： Christophe Gueret ,  Pierre Marion ,  Cecile Plain ,  Jerome Bonnardot ,  Eric Benazzi ,  Olivier Martin

    发明人： Christophe Gueret ,  Pierre Marion ,  Cecile Plain ,  Jerome Bonnardot ,  Eric Benazzi ,  Olivier Martin

    IPC分类号： C10G45/00

    CPC分类号： C10G49/007 ,  C10G2400/06

    摘要： The invention relates to a process for treating heavy petroleum feedstocks for producing a gas oil fraction that has a sulfur content of less than 50 ppm and most often 10 ppm that includes the following stages: a) ebulliated-bed catalytic hydrocracking, b) separation from hydrogen sulfide of a distillate fraction that includes a gas oil fraction and a heavier fraction than the gas oil, c) hydrotreatment of said distillate fraction, and d) separation of a gas oil fraction with less than 50 ppm of sulfur. Make-up hydrogen, preferably all make-up hydrogen, is to stage c). Advantageously, the heavier fraction from step (b) is subjected to catalytic cracking. The invention also relates to an installation that can be used for implementing this process.

    摘要翻译： 本发明涉及一种处理重质石油原料的方法，用于生产硫含量小于50ppm，最常为10ppm的瓦斯油馏分，其包括以下步骤：a）沸腾床催化加氢裂化，b） 馏出物馏分的硫化氢，其包含粗柴油馏分和比瓦斯油更重的馏分，c）加氢处理所述馏出物馏分，以及d）分离具有小于50ppm硫的粗柴油馏分。 补充氢，优选所有化妆氢，都是阶段c）。 有利地，来自步骤（b）的较重馏分经受催化裂化。 本发明还涉及可用于实现该过程的安装。

    NU-85 zeolite catalyst and a process for improving the pour point of feeds containing paraffins
    6.
    发明授权
    NU-85 zeolite catalyst and a process for improving the pour point of feeds containing paraffins 失效
    NU-85沸石催化剂和改善含有链烷烃的进料的倾点的方法

    公开(公告)号：US6153548A

    公开(公告)日：2000-11-28

    申请号：US104362

    申请日：1998-06-25

    申请人： Eric Benazzi ,  Nathalie George-Marchal ,  Christophe Gueret ,  Patrick Briot ,  Alain Billon ,  Pierre Marion

    发明人： Eric Benazzi ,  Nathalie George-Marchal ,  Christophe Gueret ,  Patrick Briot ,  Alain Billon ,  Pierre Marion

    IPC分类号： B01J29/04 ,  C01B39/02 ,  C10G45/64 ,  B01J29/74 ,  C07C5/22

    CPC分类号： C10G45/64 ,  B01J29/04 ,  C01B39/026

    摘要： The invention concerns a process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which process the feed to be treated is brought into contact with a catalyst comprising NU-85 zeolite and at least one hydro-dehydrogenating element, at a temperature which is in the range 170.degree. C. to 500.degree. C., a pressure in the range 1 to 250 bar and an hourly space velocity in the range 0.05 to 100 h.sup.-1, in the presence of hydrogen in a proportion of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils and other feeds requiring a reduction of pour point. The invention also concerns a NU-85 zeolite from which a portion of elements T (Al, Ga, Fe or B) have been removed and which has an Si/T atomic ratio of at least 18.

    摘要翻译： 本发明涉及改进含有多于10个碳原子的链烷烃的进料的倾点的方法，在该方法中待处理的进料与包含NU-85沸石和至少一种氢脱氢元素的催化剂接触 在170〜500℃的范围内，在1〜250巴的范围内的压力和0.05〜100h -1的小时空间速度，在 比例为50〜2000 l / l的饲料。 所得油具有良好的倾点和高粘度指数（VI）。 该方法也适用于需要降低倾点的瓦斯油和其他进料。 本发明还涉及一种NU-85沸石，其中元素T（Al，Ga，Fe或B）的一部分已被除去，并且Si / T原子比至少为18。

    Process for converting heavy crude oil fractions, comprising an ebullating bed conversion step and a hydrocracking step
    7.
    发明授权
    Process for converting heavy crude oil fractions, comprising an ebullating bed conversion step and a hydrocracking step 失效
    用于转化重质原油馏分的方法，包括沸腾床转化步骤和加氢裂化步骤

    公开(公告)号：US6153087A

    公开(公告)日：2000-11-28

    申请号：US103526

    申请日：1998-06-24

    申请人： Pierre-Henri Bigeard ,  Frederic Morel ,  Christophe Gueret ,  Patrick Briot ,  Pierre Marion

    发明人： Pierre-Henri Bigeard ,  Frederic Morel ,  Christophe Gueret ,  Patrick Briot ,  Pierre Marion

    IPC分类号： C10G65/12 ,  C10G69/02

    CPC分类号： C10G65/12

    摘要： A process for converting a hydrocarbon fraction comprises a step a) for treating a hydrocarbon feed in the presence of hydrogen in at least one three-phase reactor, containing at least one hydrotreatment catalyst in an ebullating bed, operating in riser mode of liquid and of gas, the reactor comprising at least one means located close to the bottom of the reactor for extracting catalyst from the reactor and at least one means located close to the top of the reactor for adding fresh catalyst to the reactor, a step b) for treating at least a portion of the effluent from step a) in the presence of hydrogen in at least one reactor containing at least one hydrocracking catalyst in a fixed bed under conditions for producing an effluent with a reduced sulphur content, and a step c) in which at least a portion of the product from step b) is sent to a distillation zone from which a gaseous fraction, a gasoline type engine fuel fraction, a diesel type engine fuel fraction and a liquid fraction which is heavier than the diesel type fraction are recovered. The process can also comprise a step d) for catalytic cracking of the heavy fraction obtained from step c).

    摘要翻译： 用于转化烃馏分的方法包括步骤a），用于在至少一个三相反应器中在氢气存在下处理烃进料，所述三相反应器在沸腾床中含有至少一种加氢处理催化剂，以液体的立管模式运行， 气体，反应器包括靠近反应器底部的至少一个装置，用于从反应器中提取催化剂和位于反应器顶部附近的至少一个装置，用于向反应器中加入新鲜的催化剂; b）用于处理 在步骤a）的至少一部分流出物在至少一个包含至少一个加氢裂化催化剂的反应器中的反应器中，在固定床中，用于生产具有降低的硫含量的流出物的条件下，步骤c），其中 将来自步骤b）的产物的至少一部分送至蒸馏区，从该蒸馏区中将气态馏分，汽油型发动机燃料馏分，柴油型发动机燃料馏分和液体馏分w 比重柴油型馏分回收重。 该方法还可以包括步骤d）用于从步骤c）获得的重馏分的催化裂化。

    Catalyst based on modified NU-87 zeolite and a process for improving the pour point of feeds containing paraffins
    8.
    发明授权
    Catalyst based on modified NU-87 zeolite and a process for improving the pour point of feeds containing paraffins 失效
    基于改性NU-87沸石的催化剂和改善含有链烷烃的进料的倾点的方法

    公开(公告)号：US6036846A

    公开(公告)日：2000-03-14

    申请号：US103522

    申请日：1998-06-24

    申请人： Eric Benazzi ,  Nathalie George-Marchal ,  Christophe Gueret ,  Patrick Briot ,  Alain Billon ,  Pierre Marion

    发明人： Eric Benazzi ,  Nathalie George-Marchal ,  Christophe Gueret ,  Patrick Briot ,  Alain Billon ,  Pierre Marion

    IPC分类号： B01J29/70 ,  C10G45/64 ,  C10G47/02

    CPC分类号： C10G45/64 ,  B01J29/70 ,  B01J2229/16 ,  B01J2229/26 ,  B01J2229/37 ,  B01J2229/42

    摘要： The invention concerns a process for improving the pour point of a feed comprising paraffins containing more than 10 carbon atoms, in which process the feed to be treated is brought into contact with a catalyst comprising an NU-87 zeolite comprising silicon and at least one clement T selected from the group formed by Al, Fe, Ga and B, from which at least a portion of clement T has been removed, and having a global Si/T ratio of over 20, the catalyst also containing at least one hydro-dehydrogenating element. The process is carried out at a temperature which is in the range 170.degree. C. to 500.degree. C., a pressure in the range 1 to 250 bar and at an hourly space velocity in the range 0.05 to 100 h.sup.-1, in the presence of hydrogen in a proportion of 50 to 2000 l/l of feed. The oils obtained have good pour points and high viscosity indices (VI). The process is also applicable to gas oils and other feeds requiring a reduction of pour point. The catalyst is also claimed.

    摘要翻译： 本发明涉及改进含有多于10个碳原子的链烷烃的进料的倾点的方法，在该方法中，待处理的进料与包含含有硅的NU-87沸石和至少一种烯键的催化剂接触 T选自由Al，Fe，Ga和B形成的基团，其中至少一部分化合物T已被除去，并且具有超过20的全局Si / T比，催化剂还含有至少一种加氢脱氢 元件。 该方法在170℃至500℃的温度，1至250巴的压力和0.05至100小时-1的小时空间速度下进行，在 以50至2000升/升饲料的比例存在氢气。 所得油具有良好的倾点和高粘度指数（VI）。 该方法也适用于需要降低倾点的瓦斯油和其他进料。 还要求催化剂。

    Process for improving aromatic and naphtheno-aromatic gas oil fractions
    10.
    发明授权
    Process for improving aromatic and naphtheno-aromatic gas oil fractions 有权
    用于改进芳族和环烷 - 芳烃瓦斯油馏分的方法

    公开(公告)号：US07381321B2

    公开(公告)日：2008-06-03

    申请号：US10367965

    申请日：2003-02-19

    申请人： Eric Benazzi ,  Patrick Bourges ,  Christophe Gueret ,  Pierre Marion

    发明人： Eric Benazzi ,  Patrick Bourges ,  Christophe Gueret ,  Pierre Marion

    IPC分类号： C10G65/12

    CPC分类号： C10G65/12

    摘要： Process for transforming a gas-oil fraction that makes it possible to produce a fuel that has a quality according to stringent requirements in terms of sulfur content, aromatic compound content, cetane number, boiling point, T95, of 95% of the compounds and density, d15/4, at 15° C. This process comprises a hydrorefining stage and a hydrocracking stage, whereby the latter uses a catalyst that contains at least one zeolite. The conversion of products that have a boiling point of less than 150° C. is, throughout the two stages of hydrocracking and hydrorefining, less than 40% by weight and, for the hydrorefining stage, between 1 and 15% by weight. The temperature, TR2, of the hydrocracking stage is less than the temperature, TR1, of the hydrorefining stage, and the variation between temperatures TR1 and TR2 is between 0 and 80° C.

    摘要翻译： 用于转化瓦斯油馏分的方法，其使得可以生产具有根据硫含量，芳香族化合物含量，十六烷值，沸点，T95的严格要求的质量为95％的化合物和密度的燃料 ，d15 / 4，在15℃。该方法包括加氢精制阶段和加氢裂化阶段，由此后者使用含有至少一种沸石的催化剂。 在加氢裂化和加氢精制两个阶段，沸点低于150℃的产物的转化率小于40重量％，加氢精制阶段为1至15重量％。 加氢裂化阶段的温度TR2小于加氢精制阶段的温度TR1，温度TR1和TR2之间的变化在0和80℃之间。