专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US07611678B2 Multi-zone moving-bed reaction device with an addition of regenerated or fresh catalyst in each zone 有权
标题翻译：多区移动床反应装置，每个区域加入再生或新鲜催化剂
公开(公告)号：US07611678B2
公开(公告)日：2009-11-03
申请号：US11269883
申请日：2005-11-09
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sancheż , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sancheż , Laurent Simon
IPC分类号： F27B15/08
CPC分类号： B01J8/125 , B01J8/085 , B01J8/087 , C10G50/00 , C10G2300/1088 , C10G2300/4018 , C10G2400/04
摘要： A reaction device includes staged zones making it possible to implement strongly endothermic or exothermic reactions. The device reduces the differences in catalytic activity between these zones using an addition of fresh or regenerated catalyst at the inlet of each reaction zone and provides an integrated heat exchanger. A process of chemical conversion employs the device for gas-phase and/or liquid-phase exothermic or endothermic reactions, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.
摘要翻译：反应装置包括分段区，可以实现强烈的吸热或放热反应。该装置通过在每个反应区的入口处添加新鲜或再生的催化剂来减少这些区域之间的催化活性的差异，并提供集成的热交换器。化学转化的方法使用该装置进行气相和/或液相放热或吸热反应，特别是为了制备柴油馏分的C2至C12馏分的低聚反应。

2. 发明申请

US20100081852A1 MULTI-ZONE FIXED-BED OR MOVING-BED REACTOR WITH AN INTEGRATED HEAT EXCHANGER 有权
标题翻译：多功能固定床或移动式反应器与集成热交换器
公开(公告)号：US20100081852A1
公开(公告)日：2010-04-01
申请号：US12572827
申请日：2009-10-02
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
IPC分类号： C07C2/04
CPC分类号： B01J8/125 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J8/085 , B01J8/087 , B01J2208/00168 , B01J2208/00203 , C10G50/00 , C10G2300/1088 , C10G2400/04
摘要： This invention relates to a staged-zone reactor of the axial-flow type that makes it possible to implement strongly endothermic or exothermic reactions. The reactor comprises a constriction of the catalytic bed between an upper zone (3a) and a lower zone (3b), making it possible to house in the reactor a heat exchanger for the intermediate heating or cooling of the effluents. Process of chemical conversion using this reactor for exothermic or endothermic reactions in the gas and/or liquid phase, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.
摘要翻译：本发明涉及一种能够实现强吸热或放热反应的轴流式分级反应器。反应器包括上部区域（3a）和下部区域（3b）之间的催化床的收缩部，使得可以在反应器中容纳用于中间加热或冷却流出物的热交换器。用于在气体和/或液相中使用该反应器进行放热或吸热反应的化学转化方法，特别是用于生产柴油馏分的C2至C12馏分的低聚反应的方法。

3. 发明申请

US20060122446A1 Multi-zone moving-bed reaction device with an addition of regenerated or fresh catalyst in each zone 有权
标题翻译：多区移动床反应装置，每个区域加入再生或新鲜催化剂
公开(公告)号：US20060122446A1
公开(公告)日：2006-06-08
申请号：US11269883
申请日：2005-11-09
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
IPC分类号： C07C2/06 , B01J8/18
CPC分类号： B01J8/125 , B01J8/085 , B01J8/087 , C10G50/00 , C10G2300/1088 , C10G2300/4018 , C10G2400/04
摘要： A reaction device with staged zones making it possible to implement strongly endothermic or exothermic reactions. The device reduces the differences in catalytic activity between these zones using an addition of fresh or regenerated catalyst at the inlet of each reaction zone and provides an integrated heat exchanger. A process of chemical conversion employs the device for gas-phase and/or liquid-phase exothermic or endothermic reactions, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.
摘要翻译：具有分段区域的反应装置可以实现强烈的吸热或放热反应。该装置通过在每个反应区的入口处添加新鲜或再生的催化剂来减少这些区域之间的催化活性的差异，并提供集成的热交换器。化学转化的方法使用该装置进行气相和/或液相放热或吸热反应，特别是为了制备柴油馏分的C2至C12馏分的低聚反应。

4. 发明申请

US20060115387A1 Multi-zone fixed-bed or moving-bed reactor with an integrated heat exchanger 有权
标题翻译：带集成热交换器的多区固定床或移动床反应器
公开(公告)号：US20060115387A1
公开(公告)日：2006-06-01
申请号：US11267570
申请日：2005-11-07
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
IPC分类号： B01J8/18
CPC分类号： B01J8/125 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J8/085 , B01J8/087 , B01J2208/00168 , B01J2208/00203 , C10G50/00 , C10G2300/1088 , C10G2400/04
摘要： This invention relates to a staged-zone reactor of the axial-flow type that makes it possible to implement strongly endothermic or exothermic reactions. The reactor comprises a constriction of the catalytic bed between an upper zone (3a) and a lower zone (3b), making it possible to house in the reactor a heat exchanger for the intermediate heating or cooling of the effluents. Process of chemical conversion using this reactor for exothermic or endothermic reactions in the gas and/or liquid phase, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.
摘要翻译：本发明涉及一种能够实现强吸热或放热反应的轴流式分级反应器。反应器包括上部区域（3a）和下部区域（3b）之间的催化床的收缩部，使得可以在反应器中容纳用于中间加热或冷却流出物的热交换器。用于在气体和/或液相中使用该反应器进行放热或吸热反应的化学转化方法，特别是用于生产柴油馏分的C2至C12馏分的低聚反应的方法。

5. 发明授权

US08609913B2 Multi-zone fixed-bed or moving-bed reactor with an integrated heat exchanger 有权
标题翻译：带集成热交换器的多区固定床或移动床反应器
公开(公告)号：US08609913B2
公开(公告)日：2013-12-17
申请号：US12572827
申请日：2009-10-02
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
IPC分类号： C07C1/00 , B01J8/00
CPC分类号： B01J8/125 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J8/085 , B01J8/087 , B01J2208/00168 , B01J2208/00203 , C10G50/00 , C10G2300/1088 , C10G2400/04
摘要： An axial flow staged zone oligomerization reaction process includes the steps of passing a hydrocarbon feedstock into the lower portion of the axial flow staged zone reactor which includes axial circulation of the hydrocarbon reaction fluid serially in each of the reaction zones, passing catalyst through a constriction zone located between successive upper and lower catalytic reaction zones which includes heat exchanging of the fluids being the constriction zone within the reactor and further includes withdrawing the oligomerized product from the top of the reactor.
摘要翻译：轴向流段分段低聚反应方法包括以下步骤：使烃原料进入轴流式分段反应器的下部，其包括在每个反应区中连续地将烃反应流体轴向循环，使催化剂通过收缩区位于连续的上部和下部催化反应区之间，其包括在反应器内作为收缩区的流体的热交换，并且还包括从反应器的顶部排出低聚产物。

6. 发明授权

US07611677B2 Multi-zone fixed-bed or moving-bed reactor with an integrated heat exchanger 有权
标题翻译：带集成热交换器的多区固定床或移动床反应器
公开(公告)号：US07611677B2
公开(公告)日：2009-11-03
申请号：US11267570
申请日：2005-11-07
申请人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
发明人： Sylvain Louret , Patrice Font , Sylvie Lacombe , Eric Sanchez , Laurent Simon
IPC分类号： F27B15/08 , B01J23/90
CPC分类号： B01J8/125 , B01J8/0453 , B01J8/0492 , B01J8/0496 , B01J8/085 , B01J8/087 , B01J2208/00168 , B01J2208/00203 , C10G50/00 , C10G2300/1088 , C10G2400/04
摘要： This invention relates to a staged-zone reactor of the axial-flow type that makes it possible to implement strongly endothermic or exothermic reactions. The reactor comprises a constriction of the catalytic bed between an upper zone (3a) and a lower zone (3b), making it possible to house in the reactor a heat exchanger for the intermediate heating or cooling of the effluents. Process of chemical conversion using this reactor for exothermic or endothermic reactions in the gas and/or liquid phase, and in particular for the oligomerization reaction of C2 to C12 fractions for the purpose of producing a diesel fraction.
摘要翻译：本发明涉及一种能够实现强吸热或放热反应的轴流式分级反应器。反应器包括上部区域（3a）和下部区域（3b）之间的催化床的收缩部，使得可以在反应器中容纳用于中间加热或冷却流出物的热交换器。用于在气体和/或液相中使用该反应器进行放热或吸热反应的化学转化方法，特别是用于生产柴油馏分的C2至C12馏分的低聚反应的方法。

7. 发明授权

US07476773B2 Process for preparing a gas oil by oligomerization 有权
标题翻译：通过低聚制备瓦斯油的方法
公开(公告)号：US07476773B2
公开(公告)日：2009-01-13
申请号：US11476203
申请日：2006-06-28
申请人： Sylvain Louret , Vincent Coupard , Laurent Simon
发明人： Sylvain Louret , Vincent Coupard , Laurent Simon
IPC分类号： C07C2/00
CPC分类号： C10G50/00
摘要： A process for preparing a gas oil cut comprises the following steps in succession: 1) oligomerizing an olefinic C2-C12 hydrocarbon cut, preferably C3-C7 and more preferably C3-C5; 2) separating the mixture of products obtained in step 1) into three cuts: a light cut containing unreacted C4 and/or C5 olefinic hydrocarbons, an intermediate cut having a T95 in the range 200-220° C. and a heavy cut comprising the complement; T95 being the temperature at which 95% by weight of product has evaporated, as determined in accordance with standard method ASTM D2887; 3) oligomerizing the intermediate cut obtained in the separation step; characterized in that in step 3), oligomerization is carried out in the presence of an olefinic C4 and/or C5 hydrocarbon cut in a weight ratio of intermediate cut to olefinic C4 and/or C5 cut in the range of 60/40 to 80/20.
摘要翻译：一种制备瓦斯油切割的方法包括以下步骤：1）使烯烃C2-C12烃馏分低聚，优选C3-C7，更优选C3-C5; 2）将步骤1）中获得的产物的混合物分成三个切口：含有未反应的C 4和/或C 5烯烃的轻馏分，T95在200-220℃范围内的中间切口，以及包含补充; T95是按照标准方法ASTM D2887测定的95重量％的产品蒸发的温度; 3）使分离步骤中获得的中间切片低聚; 其特征在于在步骤3）中，在中间切割的烯烃C4和/或C5切割重量比为60/40至80 /℃的烯烃C4和/或C5烃切割的存在下进行低聚， 20。

8. 发明申请

US20070015945A1 Process for preparing a gas oil by oligomerization 有权
标题翻译：通过低聚制备瓦斯油的方法
公开(公告)号：US20070015945A1
公开(公告)日：2007-01-18
申请号：US11476203
申请日：2006-06-28
申请人： Sylvain Louret , Vincent Coupard , Laurent Simon
发明人： Sylvain Louret , Vincent Coupard , Laurent Simon
IPC分类号： C07C2/00
CPC分类号： C10G50/00
摘要： The present invention concerns a process for preparing a gas oil cut, which comprises the following steps in succession: 1) oligomerizing an olefinic C2-C12 hydrocarbon cut, preferably C3-C7 and more preferably C3-C5; 2) separating the mixture of products obtained in step 1) into three cuts: a light cut containing unreacted C4 and/or C5 olefinic hydrocarbons, an intermediate cut having a T95 in the range 200-220° C. and a heavy cut comprising the complement; T95 being the temperature at which 95% by weight of product has evaporated, as determined in accordance with standard method ASTM D2887; 3) oligomerizing the intermediate cut obtained in the separation step; characterized in that in step 3), oligomerization is carried out in the presence of an olefinic C4 and/or C5 hydrocarbon cut.
摘要翻译：本发明涉及一种制备瓦斯油切割的方法，其包括以下步骤：1）使烯烃C2-C12烃馏分低聚，优选C 3 -C 7烃馏分，并且更优选C 3 -C 5; 2）将步骤1）中获得的产物的混合物分成三个切口：含有未反应的C 4和/或C 5烯烃的轻馏分，T95在200-220℃范围内的中间切口，以及包含补充; T95是按照标准方法ASTM D2887测定的95重量％的产品蒸发的温度; 3）使分离步骤中获得的中间切片低聚; 其特征在于在步骤3）中，在烯烃C4和/或C5烃馏分存在下进行低聚。

9. 发明授权

US08598397B2 Method for the treatment of a small-and/or medium-pore zeolite and use thereof in the oligomerisation of light olefins 有权
标题翻译：用于处理小孔和/或中孔沸石的方法及其在轻质烯烃低聚中的应用
公开(公告)号：US08598397B2
公开(公告)日：2013-12-03
申请号：US11993996
申请日：2006-06-22
申请人： Laurent Simon , Sylvie Lacombe
发明人： Laurent Simon , Sylvie Lacombe
IPC分类号： C07C2/12 , B01J29/18
CPC分类号： B01J29/06 , B01J29/18 , B01J29/65 , B01J29/7026 , B01J37/0009 , B01J2229/16 , B01J2229/186 , B01J2229/32 , B01J2229/37 , C01B39/026 , C01B39/06 , C07C2/12 , C10G50/00 , C10G2300/1088 , C10G2400/20 , C10G2400/22 , C07C11/02
摘要： Described is a process for the treatment of at least one zeolite having a pore size of less than or equal to 7 Å comprising at least a) a step for dealumination of said zeolite, b) a cationic exchange step using at least one cation other than H+, c) a step for treatment of said zeolite obtained in step b) in the presence of at least one molecular compound containing at least one silicon atom, and d) at least one heat treatment step. The present invention also concerns the preparation of a catalyst containing the zeolite treated in accordance with the treatment process the subject-matter of the invention and the use of said catalyst in a process for the oligomerization of an olefinic charge containing hydrocarbon molecules having from 2 to 12 carbon atoms per molecule.
摘要翻译：描述了一种处理至少一种孔径小于或等于7的至少一种沸石的方法，该沸石至少包括a）使所述沸石脱铝的步骤，b）使用至少一种阳离子以外的阳离子交换步骤 H +，c）在至少一种含有至少一个硅原子的分子化合物的存在下，在步骤b）中得到的所述沸石的处理步骤，和d）至少一个热处理步骤。本发明还涉及含有根据本发明主题的处理方法处理的沸石的催化剂的制备以及所述催化剂在含有烃分子的烯烃电荷低聚方法中的用途，每个分子12个碳原子。

10. 发明申请

US20080139860A1 Method for the Treatment of a Small-and/or Medium-Pore Zeolite and Use Thereof in the Oligomerisation of Light Olefins 有权
标题翻译：小分子和/或中等沸石沸石的处理方法及其在轻质烯烃低聚反应中的应用
公开(公告)号：US20080139860A1
公开(公告)日：2008-06-12
申请号：US11993996
申请日：2006-06-22
申请人： Laurent Simon , Sylvie Lacombe
发明人： Laurent Simon , Sylvie Lacombe
IPC分类号： B01J29/04 , C01B39/00 , C07C2/08
CPC分类号： B01J29/06 , B01J29/18 , B01J29/65 , B01J29/7026 , B01J37/0009 , B01J2229/16 , B01J2229/186 , B01J2229/32 , B01J2229/37 , C01B39/026 , C01B39/06 , C07C2/12 , C10G50/00 , C10G2300/1088 , C10G2400/20 , C10G2400/22 , C07C11/02
摘要： Described is a process for the treatment of at least one zeolite having a pore size of less than or equal to 7 Å comprising at least a) a step for dealumination of said zeolite, b) a cationic exchange step using at least one cation other than H+, c) a step for treatment of said zeolite obtained in step b) in the presence of at least one molecular compound containing at least one silicon atom, and d) at least one heat treatment step. The present invention also concerns the preparation of a catalyst containing the zeolite treated in accordance with the treatment process the subject-matter of the invention and the use of said catalyst in a process for the oligomerisation of an olefinic charge containing hydrocarbon molecules having from 2 to 12 carbon atoms per molecule.
摘要翻译：描述了一种处理至少一种孔径小于或等于7的至少一种沸石的方法，该沸石至少包括a）使所述沸石脱铝的步骤，b）使用至少一种阳离子以外的阳离子交换步骤 c）在至少一种含有至少一个硅原子的分子化合物的存在下处理在步骤b）中获得的所述沸石的步骤，以及d）至少一个热处理步骤。本发明还涉及含有根据本发明主题的处理方法处理的沸石的催化剂的制备，以及所述催化剂在含有烃分子的烯烃电荷的低聚方法中的用途，所述烃类分子具有2〜每个分子12个碳原子。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式