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21 条记录 (耗时 0.027 秒)

    Gasoline production by olefin polymerization
    14.
    发明申请
    Gasoline production by olefin polymerization 审中-公开
    汽油生产通过烯烃聚合

    公开(公告)号：US20060194999A1

    公开(公告)日：2006-08-31

    申请号：US11362257

    申请日：2006-02-27

    申请人： Stephen Brown ,  Georges Mathys ,  Jane Cheng ,  Jeffrey Elks ,  Ajit Dandekar ,  Benjamin Umansky ,  Michael Clark

    发明人： Stephen Brown ,  Georges Mathys ,  Jane Cheng ,  Jeffrey Elks ,  Ajit Dandekar ,  Benjamin Umansky ,  Michael Clark

    IPC分类号： C07C2/68

    CPC分类号： C10G50/00 ,  C10G2400/02

    摘要： Solid phosphoric acid (SPA) olefin oligomerization process units may be converted to operation with a more environmentally favorable solid catalyst. The SPA units in which a light olefin feed is oligomerized to form gasoline boiling range hydrocarbon product, is converted unit to operation with a molecular sieve based olefin oligomerization catalyst comprising an MWW zeolite material. Besides being more environmentally favorable in use, the MWW based zeolites offer advantages in catalyst cycle life, selectivity and product quality. After loading of the catalyst, the converted unit is operated as a fixed-bed unit by passing the C2-C4 olefinic feed to a fixed bed of the MWW zeolite condensation catalyst, typically at a temperature from 150 to 250° C., a pressure not greater than 7000 kPag, usually less than 4000 kPag and a space velocity up to 30 WHSV. The gasoline boiling range product is notable for a high level of branched chain octenes resulting in high octane quality.

    摘要翻译： 固体磷酸（SPA）烯烃低聚过程单元可以转化为具有更环保的固体催化剂的操作。 将轻烯烃进料低聚以形成汽油沸程烃产物的SPA单元通过包含MWW沸石材料的基于分子筛的烯烃低聚催化剂转化为操作。 除了在使用环境方面更有利，基于MWW的沸石提供了催化剂循环寿命，选择性和产品质量的优点。 载入催化剂后，转化的单元通过将C 2 -C 4亚烷基烯烃进料转移到MWW沸石冷凝物的固定床上作为固定床单元进行操作 催化剂，通常在150-250℃的温度下，压力不大于7000kPag，通常小于4000kPag，空速可达30WHSV。 汽油沸点范围产品对于高水平的支链辛烯是显着的，导致高辛烷值。

    Olefin oligomerization process
    18.
    发明申请
    Olefin oligomerization process 失效
    烯烃低聚方法

    公开(公告)号：US20070173676A1

    公开(公告)日：2007-07-26

    申请号：US11596170

    申请日：2005-05-26

    申请人： Stephen Brown ,  John Godsmark ,  Georges Mathys

    发明人： Stephen Brown ,  John Godsmark ,  Georges Mathys

    IPC分类号： C07C2/02

    CPC分类号： C07C2/18 ,  C07C2527/173 ,  C07C11/02

    摘要： In a process for oligomerizing an olefinic hydrocarbon feedstock, the feedstock is contacted under oligomerization conditions with (a) a first crystalline molecular sieve catalyst and (b) a second catalyst comprising a solid phosphoric acid. The first and second catalysts may be contained in separate reactors or as separate beds in a single reactor.

    摘要翻译： 在烯烃原料低聚的方法中，原料在低聚条件下与（a）第一结晶分子筛催化剂和（b）包含固体磷酸的第二催化剂接触。 第一和第二催化剂可以包含在单独的反应器中或作为单个反应器中的分离床。

    Olefin oligomerization to produce hydrocarbon compositions useful as fuels
    20.
    发明申请
    Olefin oligomerization to produce hydrocarbon compositions useful as fuels 有权
    烯烃低聚产生用作燃料的烃组合物

    公开(公告)号：US20060217580A1

    公开(公告)日：2006-09-28

    申请号：US11342385

    申请日：2006-01-27

    申请人： Keith Kuechler ,  Stephen Brown ,  Helge Jaensch ,  Georges Mathys ,  Shifang Luo ,  Jane Cheng

    发明人： Keith Kuechler ,  Stephen Brown ,  Helge Jaensch ,  Georges Mathys ,  Shifang Luo ,  Jane Cheng

    IPC分类号： C07C2/02

    CPC分类号： C10G50/00 ,  C09K8/32

    摘要： In a process for producing a hydrocarbon composition, a feed comprising at least one C3 to C8 olefin and an olefinic recycle stream rich in C9− hydrocarbons is contacted with a crystalline molecular sieve catalyst having an average crystal size no greater than 0.05 micron and an alpha value between about 100 and about 600 in at least one reaction zone under olefin oligomerization conditions including an inlet temperature between about 150° C. and about 350° C., a pressure of at least 2,860 kPa and a recycle to feed weight ratio of about 0.1 to about 3.0. The contacting produces an oligomerization effluent stream, which is separated into at least a hydrocarbon product stream rich in C9+ hydrocarbons and the olefinic recycle stream.

    摘要翻译： 在制备烃组合物的方法中，包含至少一种C 3至C 8 O烯烃的进料和富含C 9 N的烯烃循环料流 烃类与结晶分子筛催化剂接触，其结晶尺寸不大于0.05微米，在至少一个反应区域的α值为约100至约600之间，在烯烃低聚条件下，包括入口温度约为150℃ 约350℃，压力至少为2860kPa，循环至饲料重量比为约0.1至约3.0。 接触产生低聚流出物流，其被分离成至少一种富含C 9+烃的烃产物流和烯烃再循环流。