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公开(公告)号：US20140296570A1
公开(公告)日：2014-10-02
申请号：US13993194
申请日：2011-12-20
IPC分类号： C07C45/50 , C07C5/09 , C07C51/14 , C07C2/48 , C07C2/84 , C07C15/06 , C07C31/10 , C07C11/04 , C07C11/21 , C07C2/40 , C07C11/12 , C07C15/04 , C07C29/48 , C07C47/02
CPC分类号： C08F110/06 , C07C1/20 , C07C1/2076 , C07C1/24 , C07C2/403 , C07C2/48 , C07C2/76 , C07C2/84 , C07C5/09 , C07C11/04 , C07C11/12 , C07C11/21 , C07C15/04 , C07C15/06 , C07C29/16 , C07C29/48 , C07C31/10 , C07C45/505 , C07C47/02 , C07C51/14 , C08F110/02 , C10B57/16 , Y02P30/42 , C07C11/06 , C07C11/24
摘要： The invention relates to a process for converting hydrocarbons into products containing aldehydes and/or alcohols. The invention also relates to producing olefins from the aldehyde and alcohol, to polymerizing the olefins, and to equipment useful for these processes.
摘要翻译： 本发明涉及将烃转化为含有醛和/或醇的产物的方法。 本发明还涉及从醛和醇生产烯烃，使烯烃聚合，以及可用于这些方法的设备。
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32.发明申请Method and Apparatus for Managing Hydrogen Content Through The Conversion of Hydrocarbons Into Olefins 有权通过将碳氢化合物转化成烯烃来控制氢含量的方法和装置公开(公告)号：US20140163287A1
公开(公告)日：2014-06-12
申请号：US13994461
申请日：2011-12-20
IPC分类号： C07C4/04
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques combine a first hydrocarbon feed with a second hydrocarbon feed and a hydrogen (H2) containing stream to manage the hydrogen content of the feed provided to a pyrolysis reactor. The mixture is then exposed to high-severity operating conditions in a pyrolysis reactor and further processing into desired olefins.
摘要翻译： 提供了一种用于处理烃进料的装置和方法。 该方法增强了烃进料转化成转化产物，如乙烯和丙烯。 特别地，本技术结合了第一烃进料与第二烃进料和含氢（H 2）的流，以控制提供给热解反应器的进料的氢含量。 然后将混合物在热解反应器中暴露于高苛刻度的操作条件，并进一步加工成所需的烯烃。
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公开(公告)号：US08696888B2
公开(公告)日：2014-04-15
申请号：US11581882
申请日：2006-10-17
申请人： Paul F. Keusenkothen , Megan L. Renstrom , Julian A. Wolfenbarger , Stephen H. Brown , John S. Buchanan
发明人： Paul F. Keusenkothen , Megan L. Renstrom , Julian A. Wolfenbarger , Stephen H. Brown , John S. Buchanan
IPC分类号： C10G9/36
CPC分类号： B01D3/009 , C10G9/007 , C10G9/14 , C10G9/36 , C10G45/00 , C10G45/44 , C10G69/00 , C10G69/06 , C10G2300/107 , C10G2400/20 , C10G2400/30
摘要： The invention concerns integration of hydroprocessing and steam cracking. A feed comprising crude or resid-containing fraction thereof is severely hydrotreated and passed to a steam cracker to obtain an olefins product.
摘要翻译： 本发明涉及加氢处理和蒸汽裂化的整合。 包含粗制或残留物的级分的进料被严重加氢处理并通入蒸汽裂化器以获得烯烃产物。
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公开(公告)号：US20130156656A1
公开(公告)日：2013-06-20
申请号：US13768640
申请日：2013-02-15
申请人： S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
发明人： S. Mark Davis , Richard C. Stell , Jiunn-Shyan Liou , Stephen H. Brown , Paul F. Keusenkothen , Arthur R. Dinicolantonio , John J. Waldrop
IPC分类号： B01J10/00
CPC分类号： B01J10/005 , C10B55/00 , C10B55/10 , C10G9/005 , C10G9/007 , C10G9/36 , C10G51/023 , C10G2300/1077 , C10G2300/301 , C10G2300/4006 , C10G2300/807 , C10G2400/20 , C10G2400/30
摘要： This invention relates to a process and system for cracking hydrocarbon feedstock containing vacuum resid comprising: (a) subjecting a vacuum resid to a first thermal conversion in a thermal conversion reactor (such as delayed coker, fluid coker, Flexicoker™, visbreaker and catalytic hydrovisbreaker) where at least 30 wt % of the vacuum resid is converted to material boiling below 1050° F. (566° C.); (b) introducing said thermally converted resid to a vapor/liquid separator, said separator being integrated into a steam cracking furnace, to form a vapor phase and liquid phase; (c) passing said vapor phase to the radiant furnace in said steam cracking furnace; and (d) recovering at least 30 wt % olefins from the material exiting the radiant furnace (based upon the weight of the total hydrocarbon material exiting the radiant furnace).
摘要翻译： 本发明涉及一种用于裂化含有真空渣油的烃原料的方法和系统，该方法和系统包括：（a）在热转化反应器（例如延迟焦化器，流体焦化器，Flexicoker TM，减粘裂化器和 催化脱硫剂），其中至少30重量％的真空渣油转化成沸点低于1050°F（566℃）的材料; （b）将所述热转化残渣引入蒸汽/液体分离器，所述分离器整合成蒸汽裂解炉，形成气相和液相; （c）将所述气相通过所述蒸汽裂解炉中的辐射炉; 和（d）从离开辐射炉的材料（基于离开辐射炉的总烃材料的重量）回收至少30重量％的烯烃。
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35.发明授权Process and apparatus for converting high boiling point resid to light unsaturated hydrocarbons 有权将高沸点残渣转化为轻质不饱和烃的方法和设备公开(公告)号：US08440070B2
公开(公告)日：2013-05-14
申请号：US12814178
申请日：2010-06-11
申请人： Paul F. Keusenkothen
发明人： Paul F. Keusenkothen
CPC分类号： C10G9/007 , B01J8/0438 , C10G9/005 , C10G9/16 , C10G9/18 , C10G9/26 , C10G51/06 , C10G2300/107 , C10G2300/1077 , C10G2300/301
摘要： A process and apparatus process for preparing a resid-containing hydrocarbon feedstock for use in a regenerative pyrolysis reactor, comprising (a) feeding a resid-containing hydrocarbon feedstock to a thermal cracking unit; (b) thermally cracking at least about 60 wt. % of said resid having a boiling point of at least 565° C. in said hydrocarbon feedstock to form a vapor phase containing cracked hydrocarbons; (c) separating said vapor phase from remaining non-volatiles; and (d) converting the separated vapor phase in a regenerative pyrolysis reactor system.
摘要翻译： 一种用于制备用于再生热解反应器的含残余烃原料的方法和装置方法，包括（a）将含残余物的烃原料进料到热裂解单元; （b）热裂化至少约60wt。 所述残渣的％在所述烃原料中具有至少565℃的沸点以形成含有裂化烃的气相; （c）将所述气相与剩余的非挥发物分离; 和（d）在再生热解反应器系统中转化分离的气相。
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36.发明申请Process and Apparatus for Converting High Boiling Point Resid to Light Unsaturated Hydrocarbons 有权将高沸点残余物转化为轻质不饱和烃的方法和装置公开(公告)号：US20110011768A1
公开(公告)日：2011-01-20
申请号：US12814178
申请日：2010-06-11
申请人： Paul F. Keusenkothen
发明人： Paul F. Keusenkothen
CPC分类号： C10G9/007 , B01J8/0438 , C10G9/005 , C10G9/16 , C10G9/18 , C10G9/26 , C10G51/06 , C10G2300/107 , C10G2300/1077 , C10G2300/301
摘要： A process and apparatus process for preparing a resid-containing hydrocarbon feedstock for use in a regenerative pyrolysis reactor, comprising (a) feeding a resid-containing hydrocarbon feedstock to a thermal cracking unit; (b) thermally cracking at least about 60 wt. % of said resid having a boiling point of at least 565° C. in said hydrocarbon feedstock to form a vapor phase containing cracked hydrocarbons; (c) separating said vapor phase from remaining non-volatiles; and (d) converting the separated vapor phase in a regenerative pyrolysis reactor system.
摘要翻译： 一种用于制备用于再生热解反应器的含残余烃原料的方法和装置方法，包括（a）将含残余物的烃原料进料到热裂解单元; （b）热裂化至少约60wt。 所述残渣的％在所述烃原料中具有至少565℃的沸点以形成含有裂化烃的气相; （c）将所述气相与剩余的非挥发物分离; 和（d）在再生热解反应器系统中转化分离的气相。
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37.发明申请Process and System for Preparation of Hydrocarbon Feedstocks for Catalytic Cracking 有权用于催化裂化的烃原料的制备方法和系统公开(公告)号：US20110000819A1
公开(公告)日：2011-01-06
申请号：US12496037
申请日：2009-07-01
申请人： Paul F. Keusenkothen
发明人： Paul F. Keusenkothen
CPC分类号： C10G11/00 , C10G55/06 , C10G69/04 , C10G2300/107 , C10G2300/1077 , C10G2300/205 , C10G2300/301 , C10G2400/20
摘要： A process, apparatus and system for forming light olefins, the process including heating a resid-containing hydrocarbon feedstock containing at least 10 ppmw of metals to vaporize at least 90 wt. % of said hydrocarbon feedstock; separating in a knockout drum a hydrocarbon vapor portion having less than 10 ppmw metals from a non-vaporized resid-containing portion; and feeding said hydrocarbon vapor to a catalytic cracking process to form light olefins.
摘要翻译： 一种用于形成轻质烯烃的方法，装置和系统，该方法包括加热含有至少10ppmw金属的含残余烃原料以汽化至少90wt。 ％的所述烃原料; 在脱气鼓中分离具有小于10ppmw金属的烃蒸气部分，其来自未蒸发的残留物部分; 并将所述烃蒸气进料到催化裂化过程以形成轻质烯烃。
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38.发明申请公开(公告)号：US20090057200A1
公开(公告)日：2009-03-05
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： C10G9/00
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。
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39.发明申请Conversion of co-fed methane and hydrocarbon feedstocks into higher value hydrocarbons 有权将共同供应的甲烷和烃原料转化为更高价值的烃公开(公告)号：US20080300438A1
公开(公告)日：2008-12-04
申请号：US12121353
申请日：2008-05-15
CPC分类号： C10G9/26 , C10G69/06 , C10G2300/301 , C10G2300/802 , C10G2300/807 , C10G2400/20 , Y02P30/40
摘要： In one aspect, the inventive process comprises a process for pyrolyzing a hydrocarbon feedstock containing nonvolatiles in a regenerative pyrolysis reactor system. The process comprises: (a) heating the nonvolatile-containing hydrocarbon feedstock upstream of a regenerative pyrolysis reactor system to a temperature sufficient to form a vapor phase that is essentially free of nonvolatiles and a liquid phase containing the nonvolatiles; (b) separating said vapor phase from said liquid phase; (c) feeding the separated vapor phase and methane to the pyrolysis reactor system; and (d) converting the methane and separated vapor phase in said pyrolysis reactor system to form a pyrolysis product. In another aspect, the invention includes a separation process that feeds multiple pyrolysis reactors.
摘要翻译： 一方面，本发明的方法包括在再生热解反应器系统中热解含有非挥发物的烃原料的方法。 该方法包括：（a）将再生热解反应器系统上游的含非挥发物烃原料加热至足以形成基本上不含非挥发物的气相和含有非挥发物的液相的温度; （b）从所述液相中分离出所述气相; （c）将分离的气相和甲烷进料到热解反应器系统; 和（d）在所述热解反应器系统中转化甲烷和分离的气相以形成热解产物。 另一方面，本发明包括进料多个热解反应器的分离方法。
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40.发明授权公开(公告)号：US09815751B2
公开(公告)日：2017-11-14
申请号：US13993211
申请日：2011-12-20
CPC分类号： C07C5/05 , C07C2/84 , C10G3/00 , C10G9/00 , C10G45/32 , C10G57/00 , C10G69/06 , C10G70/02 , Y02P30/20
摘要： The invention relates to hydrocarbon conversion processes, e.g., to processes for producing acetylene from hydrocarbon and then hydrogenating at least a portion of the acetylene. The invention also relates to polymerizing one or more products derived from the acetylene saturation, and to equipment useful for these processes.
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