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    • 1. 发明申请
    • SEPARATION PROCESS USING AROMATIC-SELECTIVE POLYMERIC MEMBRANES
    • 使用芳族选择性聚合物膜的分离方法
    • US20080200696A1
    • 2008-08-21
    • US11428851
    • 2006-07-06
    • Jeffrey T. MillerBo ChenCraig W. CollingGeorge A. HuffBrian HenleyWilliam John KorosRaymond W. Chafin
    • Jeffrey T. MillerBo ChenCraig W. CollingGeorge A. HuffBrian HenleyWilliam John KorosRaymond W. Chafin
    • C07D209/38
    • C10G31/11B01D71/021
    • Processes are disclosed for production of value-added products from fluid admixtures of hydrocarbon compounds at least one of which is an aromatic hydrocarbon compound, by means of one or more devices using perm-selective polymeric membranes. More particularly, processes of the invention comprise separations using aromatic-selective polymeric materials comprising long-chain polymeric molecules in which recurring amide and imide linkages are part of the main polymer chain. Processes of the invention advantageously employ aromatic-selective membranes to separate an aromatic enriched stream from gaseous and/or liquid mixtures comprising one or more aromatic hydrocarbon compounds thereby producing a stream comprising the remaining compounds which may include alkenes and/or alkanes containing 3 or more carbon atoms, and/or alicyclic hydrocarbons. Processes of the invention are particularly useful for recovery of meta-xylene and para-xylene products from liquid mixtures even containing ethylbenzene as well as the three xylene isomers.
    • 公开了用于通过使用烫发选择性聚合物膜的一种或多种装置从其中至少一种为芳族烃化合物的烃化合物的流体混合物生产增值产品的方法。 更具体地,本发明的方法包括使用包含长链聚合物分子的芳族选择性聚合物材料的分离,其中重复酰胺和酰亚胺键是主要聚合物链的一部分。 本发明的方法有利地采用芳香族选择性膜从包含一种或多种芳族烃化合物的气体和/或液体混合物中分离富含芳烃的物流,从而产生包含剩余化合物的物流,其可包括含有3个或更多个的烯烃和/或烷烃 碳原子和/或脂环烃。 本发明的方法特别可用于从含有乙苯的液体混合物以及三种二甲苯异构体中回收间二甲苯和对二甲苯产物。
    • 2. 发明申请
    • Method of converting C9 aromatics-comprising mixtures to xylene isomers
    • 将C9芳族化合物混合物转化为二甲苯异构体的方法
    • US20050197518A1
    • 2005-09-08
    • US10794932
    • 2004-03-04
    • Jeffrey MillerGeorge HuffBrian Henley
    • Jeffrey MillerGeorge HuffBrian Henley
    • C07C6/12C07C15/12
    • C07C6/126Y02P20/52C07C15/08
    • Disclosed herein is a method of making xylene isomers. More specifically, the method includes contacting a C9 aromatics-comprising feed with a catalyst under conditions suitable for converting the feed to an intermediate product stream comprising xylene isomers, separating at least a portion of the xylene isomers from the intermediate product stream, and recycling to the feed the xylene isomers-lean intermediate product stream. Alternatively, the method of making xylene isomers includes contacting a feed comprising C9 aromatics and less than about 30 wt. % benzene, based on the total weight of the feed, with a non-sulfided, large-pore zeolite impregnated with a Group VIB metal oxide, under conditions suitable for converting the feed to a product stream comprising xylene isomers. The disclosed method is characterized by unexpectedly high ratios of xylene isomers to ethylbenzene, xylene isomers to C9 aromatics (e.g., methylethylbenzene), xylene isomers to C10 aromatics, trimethylbenzene to methylethylbenzene, benzene to ethylbenzene, in the product of the conversion, and the high conversion of C9 aromatics and methylethylbenzene.
    • 本文公开了制备二甲苯异构体的方法。 更具体地说,该方法包括在适于将进料转化为包含二甲苯异构体的中间产物流的条件下使含C 9芳烃的进料与催化剂接触,将至少一部分二甲苯异构体从 中间产物流,并将二氧化碳异构体贫中间产物流再循环给进料。 或者,制备二甲苯异构体的方法包括使包含C 9芳族化合物的进料和小于约30wt。 在适合于将进料转化为包含二甲苯异构体的产物流的条件下,基于进料总重量的苯与具有VIB族金属氧化物浸渍的非硫化大孔沸石。 所公开的方法的特征在于将二甲苯异构体与乙苯,二甲苯异构体到C 9芳族化合物(例如甲基乙基苯),二甲苯异构体到C 10芳烃,三甲基苯到 甲基乙基苯,苯到乙苯,转化产物和C 9 C 7芳烃和甲基乙基苯的高转化率。
    • 3. 发明申请
    • Methods of making xylene isomers
    • 制备二甲苯异构体的方法
    • US20070049780A1
    • 2007-03-01
    • US11215272
    • 2005-08-30
    • Hilary SchwartzJeffrey MillerBrian HenleyGeorge Huff
    • Hilary SchwartzJeffrey MillerBrian HenleyGeorge Huff
    • C07C4/12
    • C07C6/00C07C5/2708C07C6/126C07C2529/26Y02P20/52C07C15/08
    • Disclosed herein are methods of making xylene isomers. The methods generally include contacting an aromatics-comprising feed with a non-sulfided catalyst under conditions suitable for converting the feed to a product comprising xylene isomers. The catalyst includes a support impregnated with a hydrogenation component. The support includes a macroporous binder and a sieve selected from the group consisting of a medium pore sieve, a large pore sieve, and mixtures thereof. The selection of the sieve will depend upon the size of the molecules in the feed, intermediate, and product that can be expected from the catalytic reactions. When the molecules are expected to be large, a large pore sieve should be used. In contrast, when the molecules are expected to be smaller, either a large pore sieve, a medium pore sieve, or a mixture thereof may be used. The macropores within the support have been found to be especially beneficial because they help to overcome diffusional limitations observed when utilizing highly-active catalysts lacking such macropores.
    • 本文公开了制备二甲苯异构体的方法。 所述方法通常包括在适于将进料转化为包含二甲苯异构体的产物的条件下使包含芳烃的进料与非硫化催化剂接触。 催化剂包括浸渍有氢化组分的载体。 载体包括大孔粘合剂和选自中孔筛,大孔筛及其混合物的筛子。 筛子的选择将取决于催化反应可以预期的进料,中间体和产物中分子的大小。 当分子预期较大时,应使用大孔隙筛。 相反,当分子预期更小时,可以使用大孔隙筛孔,中孔筛或其混合物。 发现载体中的大孔是特别有益的,因为它们有助于克服当使用缺乏这种大孔的高活性催化剂时观察到的扩散限制。