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41.发明申请PROCESS FOR INCREASING METHYL TO PHENYL MOLE RATIOS AND REDUCING BENZENE CONTENT IN A MOTOR FUEL PRODUCT 有权将甲醇增加到苯酚体积比并降低电动机燃料产品中的苯含量的方法公开(公告)号：US20110174692A1
公开(公告)日：2011-07-21
申请号：US12689630
申请日：2010-01-19
申请人： Antoine Negiz , Edwin Paul Boldingh , Gregory J. Gajda , Dean E. Rende , James E. Rekoske , David E. Mackowiak , Paul Barger
发明人： Antoine Negiz , Edwin Paul Boldingh , Gregory J. Gajda , Dean E. Rende , James E. Rekoske , David E. Mackowiak , Paul Barger
CPC分类号： C10G29/205
摘要： One exemplary embodiment can be a process for increasing a mole ratio of methyl to phenyl of one or more aromatic compounds in a feed. The process can include reacting an effective amount of one or more aromatic compounds and an effective amount of one or more non-aromatic compounds to convert about 90%, by weight, of one or more C6+ non-aromatic compounds.
摘要翻译： 一个示例性实施方案可以是提高进料中一种或多种芳族化合物的甲基与苯基的摩尔比的方法。 该方法可以包括使有效量的一种或多种芳族化合物和有效量的一种或多种非芳族化合物反应，以转化约90重量％的一种或多种C 6 +非芳族化合物。
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42.发明申请公开(公告)号：US20100125037A1
公开(公告)日：2010-05-20
申请号：US12273896
申请日：2008-11-19
申请人： Antoine Negiz , Gregory J. Gajda , Dean E. Rende
发明人： Antoine Negiz , Gregory J. Gajda , Dean E. Rende
CPC分类号： B01J23/48 , B01J23/8926 , B01J23/8946 , B01J35/008 , B01J35/023 , B01J37/0221 , C07C7/163 , C07C7/167 , C10G45/34 , C10G45/40
摘要： A catalyst for selective hydrogenation of hydrocarbons is presented. The catalyst selectively hydrogenates acetylenes and diolefins to increase the monoolefins in a product stream. The catalyst includes a layered structure with an inert inner core and an outer layer bonded to the inner core, where the outer layer is a metal oxide and has at least two metals deposited on the outer layer.
摘要翻译： 提出了一种选择性氢化烃的催化剂。 催化剂选择性氢化炔烃和二烯烃以增加产物流中的单烯烃。 该催化剂包括具有惰性内芯和外层结合到内芯的层状结构，其中外层是金属氧化物并且具有沉积在外层上的至少两种金属。
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公开(公告)号：US07544848B2
公开(公告)日：2009-06-09
申请号：US12146043
申请日：2008-06-25
IPC分类号： C07C6/08
CPC分类号： C07C6/126 , C07C5/2702 , C07C6/123 , C07C15/04 , C07C15/08 , C07C2529/26 , Y02P20/125
摘要： Processes and apparatus are provided that provide high yields of xylenes per unit of aromatic-containing feed while enabling a high purity benzene co-product to be obtained without the need for an extraction or distillation to remove C6 naphthenes. The processes of this invention include a transalkylation section and a disproportionation section in the benzene and toluene-containing feed is directly provided to the transalkylation section and in which a benzene recycle loop in the transalkylation section isolates the disproportionation section from C6 naphthenes.
摘要翻译： 提供了提供每单位含芳族化合物的高产率的二甲苯的方法和装置，同时能够获得高纯度苯共同产物，而不需要萃取或蒸馏除去C6环烷烃。 本发明的方法包括烷基转移部分和苯和含甲苯的进料中的歧化部分直接提供给烷基转移部分，其中烷基转移部分中的苯循环回路将歧化部分与C6环烷烃隔离。
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公开(公告)号：US07396966B2
公开(公告)日：2008-07-08
申请号：US11313071
申请日：2005-12-20
CPC分类号： C07C15/107 , C07C2/66
摘要： Aromatic by-products are sorbed from mono-olefin-containing feedstocks of olefins having from about 6 to 22 carbon atoms per molecule that contain aromatic by-products having from 7 to 22 carbon atoms per molecule. A benzene-containing regenerant displaces and desorbs the aromatic by-products from the sorbent and a regeneration effluent is provided. The regeneration effluent is treated in a regeneration effluent distillation system to provide a benzene-rich stream and an aromatic by-products-containing stream. The latter is subjected to benzene-forming conditions and recycled to the regeneration effluent distillation system where benzene is recovered.
摘要翻译： 芳族副产物被从每分子含有约6至22个碳原子的含单烯烃的原料中吸收，每分子含有7至22个碳原子的芳族副产物。 含苯的再生剂从吸附剂中取代并解吸芳族副产物，并提供再生流出物。 再生流出物在再生流出物蒸馏系统中处理以提供富含苯的流和含芳香族副产物的流。 后者经受苯形成条件并再循环至回收苯的再生流出物蒸馏系统。
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45.发明申请Processes for Producing Xylenes Using Isomerization and Transalkylation Reactions and Apparatus Therefor 失效使用异构化和烷基转移反应生产二甲苯的方法及其设备公开(公告)号：US20080067053A1
公开(公告)日：2008-03-20
申请号：US11945617
申请日：2007-11-27
申请人： Antoine Negiz , James Rekoske , Edwin Boldingh
发明人： Antoine Negiz , James Rekoske , Edwin Boldingh
IPC分类号： B01D3/14
CPC分类号： B01J8/0457 , B01J8/0453 , B01J8/0492 , B01J2219/00006 , C07C6/126 , C07C15/08
摘要： Processes for making xylene isomer using integrated transalkylation and isomerization reaction zones to enhance xylene recovery and enable reduction in capital costs and energy consumption.
摘要翻译： 使用整合的烷基转移反应区和异构化反应区制备二甲苯异构体的方法，以增强二甲苯回收率，并降低资本成本和能源消耗。
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公开(公告)号：US20070042905A1
公开(公告)日：2007-02-22
申请号：US11550823
申请日：2006-10-19
申请人： Antoine Negiz , Edwin Boldingh , Sergio Pischek
发明人： Antoine Negiz , Edwin Boldingh , Sergio Pischek
CPC分类号： C07C6/126 , C07C2521/04 , C07C2521/12 , C07C2523/08 , C07C2523/14 , C07C2523/36 , C07C2523/40 , C07C2523/745 , C07C2523/75 , C07C2523/755 , C07C2529/18 , C07C2529/70 , C07C2529/85
摘要： A transalkylation process for reacting carbon number nine aromatics with toluene to form carbon number eight aromatics such as para-xylene is herein disclosed. The process is based on the discovery that deactivating contaminants present in typical hydrocarbon feeds, such as chlorides, can be removed with an alumina guard bed prior to contacting with a transalkylation catalyst. Effective transalkylation catalysts have a solid-acid component such as mordenite, and a metal component such as rhenium. The invention is embodied in a process, a catalyst system, and an apparatus. The invention provides for longer catalyst cycle life when processing aromatics under commercial transalkylation conditions.
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公开(公告)号：US08926829B2
公开(公告)日：2015-01-06
申请号：US13416513
申请日：2012-03-09
申请人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
发明人： Manuela Serban , Antoine Negiz , Kurt M. VandenBussche , Mark D. Moser , David A. Wegerer , Gregory J. Gajda
IPC分类号： C10G35/04 , C10G35/06 , C10G35/085 , C10G59/06
CPC分类号： C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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公开(公告)号：US08679321B2
公开(公告)日：2014-03-25
申请号：US13416577
申请日：2012-03-09
IPC分类号： C10G59/02
CPC分类号： C07C2/76 , C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
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公开(公告)号：US20120273392A1
公开(公告)日：2012-11-01
申请号：US13428005
申请日：2012-03-23
IPC分类号： C10G59/02
CPC分类号： C07C2/76 , C10G59/02 , C10G69/08 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译： 提出了一种重整烃流的方法。 该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。 改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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公开(公告)号：US20100331171A1
公开(公告)日：2010-12-30
申请号：US12493415
申请日：2009-06-29
申请人： Gregory J. Gajda , Bryan K. Glover , Antoine Negiz , Mark G. Riley , John J. Senetar , Erik M. Holmgreen
发明人： Gregory J. Gajda , Bryan K. Glover , Antoine Negiz , Mark G. Riley , John J. Senetar , Erik M. Holmgreen
CPC分类号： B01J23/40 , B01J23/44 , B01J23/58 , B01J23/66 , B01J35/002 , B01J35/008 , B01J35/023 , B01J37/0205 , B01J37/0221 , B01J37/0242 , B01J37/08 , B01J37/18 , C07C7/163 , C07C7/167 , C10G45/40 , Y02P20/52 , C07C11/04
摘要： A process and catalyst for use in the selective hydrogenation of acetylene to ethylene is presented. The catalyst comprises a layered structure, wherein the catalyst has an inner core and an outer layer of active material. The catalyst further includes a metal deposited on the outer layer, and the catalyst is formed such that the catalyst has an accessibility index between 3 and 500.
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