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41. 发明授权

US07867379B2 Production of an upgraded stream from steam cracker tar by ultrafiltration 有权
标题翻译：通过超滤从蒸汽裂解焦油生产升级的流
公开(公告)号：US07867379B2
公开(公告)日：2011-01-11
申请号：US11980162
申请日：2007-10-30
申请人： Daniel P. Leta , Edward W. Corcoran , Eric B. Sirota , Stephen M. Cundy , Kirk C. Nadler , John Di-Yi Ou , Paul F. Keusenkothen
发明人： Daniel P. Leta , Edward W. Corcoran , Eric B. Sirota , Stephen M. Cundy , Kirk C. Nadler , John Di-Yi Ou , Paul F. Keusenkothen
IPC分类号： B01D61/16 , C10G9/36
CPC分类号： C10G55/04 , C10G31/11
摘要： This invention relates to a process of producing an upgraded product stream from steam cracker tar feedstream suitable for use in refinery or chemical plant processes or for utilization in fuel oil sales or blending. This process utilizes an ultrafiltration process for separating the steam cracker tar constituents resulting in a high recovery, low-energy process with improved separation and product properties.
摘要翻译：本发明涉及一种从适用于炼油厂或化工厂工艺的蒸汽裂解塔焦油原料生产升级产品流的方法或用于燃料油销售或混合的方法。该方法利用超滤方法分离蒸汽裂解焦油成分，导致高回收率，低能量的方法，具有改进的分离和产物性能。

42. 发明授权

US07199273B2 Selective hydrogenation of alkynes and/or diolefins 失效
标题翻译：炔和/或二烯烃的选择性氢化
公开(公告)号：US07199273B2
公开(公告)日：2007-04-03
申请号：US10721046
申请日：2003-11-24
申请人： Michel Molinier , John Di-Yi Ou , Michael A. Risch
发明人： Michel Molinier , John Di-Yi Ou , Michael A. Risch
IPC分类号： B01J31/00 , C07C7/163
CPC分类号： B01J37/0203 , B01J23/40 , B01J23/62 , B01J23/74 , B01J23/896 , C07C5/05 , C07C5/09 , C07C7/163 , C07C7/167 , C07C2521/04 , C07C2523/62
摘要： A process for selectively removing alkynes and/or diolefins from a feedstock also containing olefins comprises contacting the feedstock with hydrogen in the presence of a catalyst composition. The catalyst composition comprises at least one metal component selected from Groups 8 to 10 of the Periodic Table of Elements impregnated on a support, wherein an organic nitrogen-containing compound is contacted with the support before, during or after the metal impregnation.
摘要翻译：从还含有烯烃的原料中选择性除去炔烃和/或二烯烃的方法包括在催化剂组合物存在下使原料与氢气接触。催化剂组合物包含至少一种选自浸渍在载体上的元素周期表第8至10组的金属组分，其中有机含氮化合物在金属浸渍之前，期间或之后与载体接触。

43. 发明授权

US06987208B2 Process for removing oxygenates from an olefinic stream 失效
标题翻译：从烯烃流中除去含氧化合物的方法
公开(公告)号：US06987208B2
公开(公告)日：2006-01-17
申请号：US10761873
申请日：2004-01-21
申请人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
发明人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
IPC分类号： C07C1/20 , C07C7/48
CPC分类号： C07C7/14841 , C07C11/02
摘要： The present invention provides a process for removing oxygenate impurities, e.g., dimethyl ether, from an olefinic product stream by converting the oxygenate impurity to a compound whose boiling point differs by at least about 5° C. from the oxygenate impurity. Typically, the compound is more readily removable from the product stream than the oxygenate impurity.
摘要翻译：本发明提供了通过将含氧化合物杂质转化为沸点与含氧化合物杂质相差至少约5℃的化合物，从烯烃产物流中除去含氧化合物杂质如二甲醚的方法。通常，化合物比含氧化合物杂质更容易从产物流中除去。

44. 发明授权

US06878855B2 Process for producing para-xylene 失效
标题翻译：生产对二甲苯的方法
公开(公告)号：US06878855B2
公开(公告)日：2005-04-12
申请号：US09791300
申请日：2001-02-22
申请人： Harry W. Deckman , Ronald Richard Chance , John Di-Yi Ou , James Alexander McHenry , Juan José Reinoso
发明人： Harry W. Deckman , Ronald Richard Chance , John Di-Yi Ou , James Alexander McHenry , Juan José Reinoso
IPC分类号： C07B61/00 , C07C5/27 , C07C7/13 , C07C15/08 , C07C5/22
CPC分类号： C07C15/08 , C07C5/2708 , C07C7/13 , C07C2529/04 , C07C15/067
摘要： A process and a system for increasing para-xylene production from a C8 aromatic feedstream by coupling at least one xylene isomerization reactor with at least one pressure swing adsorption unit or temperature swing absorption unit to produce a product having a super-equilibrium para-xylene concentration. This product is then subjected to para-xylene separation and purification.
摘要翻译：通过将至少一个二甲苯异构化反应器与至少一个变压吸附单元或温度摆动吸收单元联接以产生具有超平衡对二甲苯浓度的产物，从C8芳族原料流增加对二甲苯生产的方法和系统。然后将该产物进行对二甲苯分离和纯化。

45. 发明授权

US06717025B1 Process for removing oxygenates from an olefinic stream 失效
标题翻译：从烯烃流中除去含氧化合物的方法
公开(公告)号：US06717025B1
公开(公告)日：2004-04-06
申请号：US10295066
申请日：2002-11-15
申请人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
发明人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
IPC分类号： C07C7148
CPC分类号： C07C7/14841 , C07C11/02
摘要： The present invention provides a process for removing oxygenate impurities, e.g., dimethyl ether, from an olefinic product stream by converting the oxygenate impurity to a compound whose boiling point differs by at least about 5° C. from the oxygenate impurity. Typically, the compound is more readily removable from the product stream than the oxygenate impurity.
摘要翻译：本发明提供了通过将含氧化合物杂质转化为沸点与含氧化合物杂质相差至少约5℃的化合物，从烯烃产物流中除去含氧化合物杂质如二甲醚的方法。通常，化合物比含氧化合物杂质更容易从产物流中除去。

46. 发明授权

US06489527B1 Process for improving purity of para-xylene product 失效
标题翻译：提高对二甲苯产品纯度的方法
公开(公告)号：US06489527B1
公开(公告)日：2002-12-03
申请号：US08575443
申请日：1995-12-20
申请人： John Di-Yi Ou , Harold William Helmke , Dana Lynn Pilliod
发明人： John Di-Yi Ou , Harold William Helmke , Dana Lynn Pilliod
IPC分类号： C07C266
CPC分类号： C07C7/14875 , C07C7/005 , C07C7/14883 , Y02P20/52 , C07C15/08
摘要： A process for producing 99.5+ wt. % para-xylene by selective alkylation has been discovered. A mixure of isomers of para-xylene having at least about 90.0 wt. % purity may be reacted with an alkylating agent having at least one tertiary butyl moiety in the presence of an acidic catalyst under conditions where the catalyst is in good molecular contact with the non-para-xylene isomers. The catalyst may be a high surface area acidic heterogeneous catalyst such as a proton-exchanged zeolite. Upon distillation, para-xylene is recovered in 99.5 wt. % purity or higher. The selective alkylation gives little or no alkylation of the para-xylene, the most predominant species, and very little or no isomerization to the other, non-desirable isomers.
摘要翻译：一种生产99.5重量％已经发现通过选择性烷基化的％对二甲苯。对二甲苯异构体的混合物具有至少约90.0wt。在催化剂与非对二甲苯异构体分子接触良好的条件下，可以在酸性催化剂存在下，将纯度的％与具有至少一个叔丁基部分的烷基化剂反应。催化剂可以是高表面积的酸性非均相催化剂，例如质子交换的沸石。蒸馏后，在99.5wt。％纯度或更高。选择性烷基化几乎不产生对二甲苯（最主要的物质）的烷基化，并且很少或没有异构化到另一种非期望的异构体。

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