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    Production of high purity cumene from non-extracted feed and hydrocarbon composition useful therein
    31.
    发明申请
    Production of high purity cumene from non-extracted feed and hydrocarbon composition useful therein 有权
    从非提取的原料和可用于其中的烃组合物生产高纯度枯烯

    公开(公告)号：US20080194890A1

    公开(公告)日：2008-08-14

    申请号：US11705323

    申请日：2007-02-12

    申请人： Stephen Harold Brown

    发明人： Stephen Harold Brown

    IPC分类号： C07C2/66

    CPC分类号： C07C15/085 ,  C07C2/66 ,  C07C2529/70

    摘要： A process for producing an cumene product having a purity of at least 99.50 percent based on the weight of cumene present in the product by the propylation of the benzene present in non-extracted hydrocarbon composition feed, e.g., non-extracted reformate. The non-extracted hydrocarbon composition feed is substantially free of both C4− hydrocarbons and the C7+ aromatic hydrocarbons and contains benzene and benzene coboilers. The process is carried out in the liquid phase, in the presence of an acid-active catalyst containing MCM-22 family molecular sieve, and under specified conditions.

    摘要翻译： 基于存在于产物中的异丙苯的重量，通过非萃取的烃组合物进料例如未提取的重整油中存在的苯的丙基，生产纯度至少为99.50％的异丙基苯产品的方法。 未提取的烃组合物进料基本上不含C 4+烃和C 7+芳烃，并且含有苯和苯共沸混合物。 该方法在液相中，在含有MCM-22族分子筛的酸活性催化剂存在下，并在规定的条件下进行。

    Olefin oligomerization
    32.
    发明授权
    Olefin oligomerization 有权
    烯烃低聚

    公开(公告)号：US07183450B2

    公开(公告)日：2007-02-27

    申请号：US10201203

    申请日：2002-07-22

    申请人： Stephen Harold Brown ,  Georges M. K. Mathys

    发明人： Stephen Harold Brown ,  Georges M. K. Mathys

    IPC分类号： C07C1/20

    CPC分类号： C07C2/12 ,  C07C2527/173 ,  C07C2529/08 ,  C07C2529/18 ,  C07C2529/40 ,  C07C2529/50

    摘要： This invention is to a method of oligomerizing an olefin feed stream. The olefin feed stream contains at least one C2 to C12 olefin to obtain an olefin feed stream and has from about 1,000 ppm to about 10 percent by weight oxygenated hydrocarbon. The olefin is oligomerized by contacting with an acid based oligomerization catalyst.

    摘要翻译： 本发明是一种使烯烃进料流低聚的方法。 烯烃进料流含有至少一个C 12 C 12 C 12 C 12烯烃，以获得烯烃进料流，并具有约1,000ppm至约10重量％的氧化烃。 通过与酸基低聚催化剂接触来使烯烃低聚。

    Process of manufacturing para-xylene
    38.
    发明授权
    Process of manufacturing para-xylene 失效
    对二甲苯生产工艺

    公开(公告)号：US07629498B2

    公开(公告)日：2009-12-08

    申请号：US11823584

    申请日：2007-06-28

    申请人： Stephen Harold Brown ,  John Scott Buchanan

    发明人： Stephen Harold Brown ,  John Scott Buchanan

    IPC分类号： C07C2/66

    CPC分类号： C07C4/04 ,  C07C1/24 ,  C07C6/126 ,  C07C15/08

    摘要： This disclosure relates to a process of manufacturing para-xylene, comprising (a) contacting a pygas feedstock and methylating agent with a catalyst under reaction conditions to produce a product having para-xylene, wherein the product has higher para-xylene content than the para-xylene content of the pygas feedstock; and (b) separating the para-xylene from the product of the step (a), wherein the catalyst comprises a molecular sieve having a Diffusion Parameter for 2,2-dimethylbutane of about 0.1-15 sec−1 when measured at a temperature of 120° C. and a 2,2-dimethylbutane pressure of 8 kPa-a and the pygas comprises from about 1 to about 65 wt % benzene and from about 5 to 35 wt % toluene.

    摘要翻译： 本公开涉及一种制备对二甲苯的方法，其包括（a）在反应条件下使炽热原料和甲基化剂与催化剂接触以产生具有对二甲苯的产物，其中该产物比对位二甲苯​​具有更高的对二甲苯含量 焦炭原料的二甲苯含量; 和（b）从步骤（a）的产物中分离对二甲苯，其中当在下列温度下测量时，催化剂包含具有约0.1-15秒-1的2,2-二甲基丁烷扩散参数的分子筛 120℃，并且2,2-二甲基丁烷压力为8kPa-a，焦煤包含约1至约65重量％的苯和约5至35重量％的甲苯。