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    High purity olefinic naphthas for the production of ethylene and propylene
    2.
    发明授权
    High purity olefinic naphthas for the production of ethylene and propylene 失效
    用于生产乙烯和丙烯的高纯度烯烃石脑油

    公开(公告)号：US07431821B2

    公开(公告)日：2008-10-07

    申请号：US10355110

    申请日：2003-01-31

    申请人： Dennis J. O'Rear ,  Guan Dao Lei

    发明人： Dennis J. O'Rear ,  Guan Dao Lei

    IPC分类号： C10L1/04

    CPC分类号： C10G2/32 ,  C10L1/06

    摘要： The present invention relates to an olefinic naphtha and a process for producing lower olefinc from this naphtha. In the process of the present invention for producing lower olefins, preferably ethylene, at least a portion of a hydrocarbon asset is converted to synthesis gas and at least a portion of the synthesis gas is converted to an olefinic naphtha by a Fischer-Tropsch process. At least a portion of the olefinic naphtha is converted in a naphtha cracker to a product stream comprising lower olefins, and at least a portion of the lower olefins from the product stream of the cracker are recovered.

    摘要翻译： 本发明涉及一种烯烃石脑油以及由该石脑油生产低级烯烃的方法。 在用于生产低级烯烃（优选乙烯）的本发明的方法中，烃资产的至少一部分转化为合成气，并且通过费 - 托法将至少一部分合成气转化为烯烃石脑油。 将至少一部分烯烃石脑油在石脑油裂解装置中转化成包含低级烯烃的产物流，并且从裂化器的产物流中回收至少一部分低级烯烃。

    High purity olefinic naphthas for the production of ethylene and propylene
    3.
    发明授权
    High purity olefinic naphthas for the production of ethylene and propylene 有权
    用于生产乙烯和丙烯的高纯度烯烃石脑油

    公开(公告)号：US07150821B2

    公开(公告)日：2006-12-19

    申请号：US10355158

    申请日：2003-01-31

    申请人： Dennis J. O'Rear ,  Guan Dao Lei

    发明人： Dennis J. O'Rear ,  Guan Dao Lei

    IPC分类号： C10G9/00 ,  C07C1/04

    CPC分类号： C07C4/02 ,  C10G2400/02 ,  C10G2400/20 ,  C07C11/04

    摘要： The present invention relates to an olefinic naphtha and a process for producing lower olefins from this naphtha. In the process of the present invention for producing lower olefins, preferably ethylene, at least a portion of a hydrocarbon asset is converted to synthesis gas and at least a portion of the synthesis gas is converted to an olefinic naphtha by a Fischer-Tropsch process. At least a portion of the olefinic naphtha is converted in a naphtha cracker to a product stream comprising lower olefins, and at least a portion of the lower olefins from the product stream of the naphtha cracker are recovered.

    摘要翻译： 本发明涉及一种烯烃石脑油以及由该石脑油生产低级烯烃的方法。 在用于生产低级烯烃（优选乙烯）的本发明的方法中，烃资产的至少一部分转化为合成气，并且通过费 - 托法将至少一部分合成气转化为烯烃石脑油。 将至少一部分烯烃石脑油在石脑油裂解装置中转化成包含低级烯烃的产物流，并回收至少一部分来自石脑油裂化装置的产物流的低级烯烃。

    Process for the oligomerization of olefins in fischer-tropsch derived condensate feed
    4.
    发明申请
    Process for the oligomerization of olefins in fischer-tropsch derived condensate feed 审中-公开
    在费托衍生的冷凝物进料中烯烃低聚的方法

    公开(公告)号：US20060149107A1

    公开(公告)日：2006-07-06

    申请号：US11372531

    申请日：2006-03-10

    申请人： Thomas Harris ,  Michael Cheng ,  Guan-Dao Lei

    发明人： Thomas Harris ,  Michael Cheng ,  Guan-Dao Lei

    IPC分类号： C07C2/02

    CPC分类号： C10G50/00 ,  C10G2/32 ,  C10G25/03 ,  C10G50/02 ,  C10G57/02

    摘要： A process for oligomerizing the olefins present in a Fischer-Tropsch derived condensate containing a mixture of olefins and oxygenates and boiling in the range of diesel which comprises (a) removing substantially all of the oxygenates present in the Fischer-Tropsch condensate; (b) contacting the Fischer-Tropsch derived condensate having less than 100 ppmw elemental oxygen with an ionic liquid catalyst in an oligomerization zone under oligomerization reaction conditions; and (c) recovering from the oligomerization zone a Fischer-Tropsch derived product having molecules characterized by a higher average molecular weight and increased branching as compared to the Fischer-Tropsch derived condensate.

    摘要翻译： 一种使包含烯烃和含氧化合物的混合物的费 - 托衍生的缩合物中存在的烯烃低聚的方法，其在柴油范围内沸腾，其包括（a）基本上除去费 - 托冷凝物中存在的基本上所有的含氧化合物; （b）在低聚反应条件下，将低于100ppmw的元素氧的费 - 托衍生的缩合物与低聚区的离子液体催化剂接触; 和（c）与费 - 托衍生的缩合物相比，从低聚区回收具有分子特征在于具有较高平均分子量和增加的支化的费 - 托衍生产物。

    LUBRICATING BASE OIL PRODUCTION
    6.
    发明申请
    LUBRICATING BASE OIL PRODUCTION 审中-公开
    润滑基油生产

    公开(公告)号：US20150136646A1

    公开(公告)日：2015-05-21

    申请号：US14541684

    申请日：2014-11-14

    申请人： Bi-Zeng Zhan ,  Horacio Trevino ,  Theodorus Ludovicus Michael Maesen ,  Guan-Dao Lei

    发明人： Bi-Zeng Zhan ,  Horacio Trevino ,  Theodorus Ludovicus Michael Maesen ,  Guan-Dao Lei

    IPC分类号： C10M101/02 ,  C10G67/02

    CPC分类号： C10M101/02 ,  C10G47/06 ,  C10G65/12 ,  C10G67/02

    摘要： A process is provided for producing a heavy lubricating base oil by hydrocracking a lubricating oil feedstock at high yield. The lubricating oil feedstock contains a hydroprocessed stream that is difficult to process using a conventional catalyst system. The catalyst used in the process includes a mixed metal sulfide catalyst that comprises at least one Group VIB metal and at least one Group VIII metal. The process also provides for hydroisomerization and hydrofinishing process steps to prepare the lubricating base oil.

    摘要翻译： 提供了一种通过以高产率加氢裂化润滑油原料来生产重质润滑基础油的方法。 润滑油原料含有使用常规催化剂体系难以加工的加氢处理流。 在该方法中使用的催化剂包括含有至少一种VIB族金属和至少一种第Ⅷ族金属的混合金属硫化物催化剂。 该方法还提供加氢异构化和加氢处理步骤以制备润滑基础油。

    Catalytic processes and systems for base oil production from light feedstock
    7.
    发明授权
    Catalytic processes and systems for base oil production from light feedstock 有权
    从轻原料生产基础油的催化过程和系统

    公开(公告)号：US08617387B2

    公开(公告)日：2013-12-31

    申请号：US13159634

    申请日：2011-06-14

    申请人： Kamala Krishna ,  Guan-Dao Lei

    发明人： Kamala Krishna ,  Guan-Dao Lei

    IPC分类号： C10G35/04

    CPC分类号： B01J29/74 ,  B01J21/12 ,  B01J23/42 ,  B01J23/44 ,  B01J35/0006 ,  B01J2229/20 ,  B01J2229/42 ,  C10G45/10 ,  C10G45/64 ,  C10G65/043 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/4025 ,  C10G2400/10

    摘要： Processes and catalyst systems are provided for dewaxing a light hydrocarbon feedstock to form a lubricant base oil. A layered catalyst system of the present invention may comprise a first hydroisomerization dewaxing catalyst disposed upstream from a second hydroisomerization dewaxing catalyst. Each of the first and second hydroisomerization dewaxing catalysts may be selective for the isomerization of n-paraffins. The first hydroisomerization catalyst may have a higher level of selectivity for the isomerization of n-paraffins than the second hydroisomerization dewaxing catalyst.

    摘要翻译： 提供了工艺和催化剂体系，用于脱蜡轻烃原料以形成润滑剂基础油。 本发明的层状催化剂体系可以包含设置在第二加氢异构化脱蜡催化剂上游的第一加氢异构化脱蜡催化剂。 第一和第二加氢异构化脱蜡催化剂中的每一种可以是正链烷烃异构化的选择性。 与第二加氢异构化脱蜡催化剂相比，第一加氢异构化催化剂对正链烷烃的异构化可具有更高的选择性。

    CATALYTIC PROCESSES AND SYSTEMS FOR BASE OIL PRODUCTION FROM HEAVY FEEDSTOCK
    8.
    发明申请
    CATALYTIC PROCESSES AND SYSTEMS FOR BASE OIL PRODUCTION FROM HEAVY FEEDSTOCK 有权
    催化工艺和系统从重型饲料生产基础油

    公开(公告)号：US20110315597A1

    公开(公告)日：2011-12-29

    申请号：US13159665

    申请日：2011-06-14

    申请人： Kamala Krishna ,  Guan-Dao Lei

    发明人： Kamala Krishna ,  Guan-Dao Lei

    IPC分类号： C10G49/02 ,  B01J29/04 ,  C10G49/06

    CPC分类号： B01J29/74 ,  B01J23/58 ,  B01J29/70 ,  B01J37/0201 ,  B01J37/0244 ,  B01J2229/42 ,  C10G45/64 ,  C10G65/043 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/4025 ,  C10G2400/10

    摘要： Processes and catalyst systems are provided for dewaxing a heavy hydrocarbon feedstock to form a lubricant base oil. A layered catalyst system of the present invention may comprise a first hydroisomerization dewaxing catalyst disposed upstream from a second hydroisomerization dewaxing catalyst. Each of the first and second hydroisomerization dewaxing catalysts may be selective for the isomerization of n-paraffins. The first hydroisomerization catalyst has a first level of selectivity for the isomerization of n-paraffins, the second hydroisomerization dewaxing catalyst has a second level of selectivity for the isomerization of n-paraffins, and a layered catalyst system comprising the first and second hydroisomerization dewaxing catalysts has a third level of selectivity for the isomerization of n-paraffins. The third level of selectivity may be higher than each of the first level of selectivity and the second level of selectivity.

    摘要翻译： 提供了用于脱蜡重烃原料以形成润滑剂基础油的方法和催化剂体系。 本发明的层状催化剂体系可以包含设置在第二加氢异构化脱蜡催化剂上游的第一加氢异构化脱蜡催化剂。 第一和第二加氢异构化脱蜡催化剂中的每一种可以是正链烷烃异构化的选择性。 第一加氢异构化催化剂对正链烷烃的异构化具有第一水平的选择性，第二加氢异构化脱蜡催化剂对于正链烷烃的异构化具有第二水平的选择性，以及包含第一和第二加氢异构化脱蜡催化剂的层状催化剂体系 对正链烷烃的异构化具有第三级选择性。 第三级选择性可能高于第一级选择性和第二级选择性。

    CATALYTIC PROCESSES AND SYSTEMS FOR BASE OIL PRODUCTION FROM HEAVY FEEDSTOCK
    10.
    发明申请
    CATALYTIC PROCESSES AND SYSTEMS FOR BASE OIL PRODUCTION FROM HEAVY FEEDSTOCK 审中-公开
    催化工艺和系统从重型饲料生产基础油

    公开(公告)号：US20130260985A1

    公开(公告)日：2013-10-03

    申请号：US13905230

    申请日：2013-05-30

    申请人： Kamala Raghunathan Krishna ,  Guan-Dao Lei

    发明人： Kamala Raghunathan Krishna ,  Guan-Dao Lei

    IPC分类号： B01J29/74

    CPC分类号： B01J29/74 ,  B01J23/58 ,  B01J29/70 ,  B01J37/0201 ,  B01J37/0244 ,  B01J2229/42 ,  C10G45/64 ,  C10G65/043 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/304 ,  C10G2300/4025 ,  C10G2400/10

    摘要： A catalyst system is provided for dewaxing a heavy hydrocarbon feedstock to form a lubricant base oil. A layered catalyst system of the present invention may comprise a first hydroisomerization dewaxing catalyst disposed upstream from a second hydroisomerization dewaxing catalyst. Each of the first and second hydroisomerization dewaxing catalysts may be selective for the isomerization of n-paraffins. The first hydroisomerization catalyst has a first level of selectivity for the isomerization of n-paraffins, the second hydroisomerization dewaxing catalyst has a second level of selectivity for the isomerization of n-paraffins, and a layered catalyst system comprising the first and second hydroisomerization dewaxing catalysts has a third level of selectivity for the isomerization of n-paraffins. The third level of selectivity may be higher than each of the first level of selectivity and the second level of selectivity.

    摘要翻译： 提供催化剂体系用于脱蜡重质烃原料以形成润滑剂基础油。 本发明的层状催化剂体系可以包含设置在第二加氢异构化脱蜡催化剂上游的第一加氢异构化脱蜡催化剂。 第一和第二加氢异构化脱蜡催化剂中的每一种可以是正链烷烃异构化的选择性。 第一加氢异构化催化剂对正链烷烃的异构化具有第一水平的选择性，第二加氢异构化脱蜡催化剂对于正链烷烃的异构化具有第二水平的选择性，以及包含第一和第二加氢异构化脱蜡催化剂的层状催化剂体系 对正链烷烃的异构化具有第三级选择性。 第三级选择性可能高于第一级选择性和第二级选择性。