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1. 发明申请

US20140163271A1 Hydrocarbon Conversion Process 有权
标题翻译：烃转化过程
公开(公告)号：US20140163271A1
公开(公告)日：2014-06-12
申请号：US13993211
申请日：2011-12-20
申请人： Paul F. Keusenkothen , Hershkowitz Frank
发明人： Paul F. Keusenkothen , Hershkowitz Frank
IPC分类号： C07C5/05 , C07C2/84
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.
摘要翻译：本发明涉及烃转化方法，例如用于从烃生产乙炔，然后氢化至少一部分乙炔的方法。本发明还涉及聚合一种或多种衍生自乙炔饱和度的产物和用于这些方法的设备。

2. 发明授权

US09315430B2 Reactor components 有权
标题翻译：反应器组件
公开(公告)号：US09315430B2
公开(公告)日：2016-04-19
申请号：US13658851
申请日：2012-10-24
申请人： Paul F. Keusenkothen , Frank Hershkowitz , Gary D. Mohr , ChangMin Chun , Jeffrey W. Frederick
发明人： Paul F. Keusenkothen , Frank Hershkowitz , Gary D. Mohr , ChangMin Chun , Jeffrey W. Frederick
IPC分类号： C07C4/04 , C07C4/02 , C07C2/02 , C07C11/00 , F23L15/02 , B01J19/02 , B01J19/24 , B01J4/00 , B01J8/04 , C10G9/18 , C10G9/26 , B01J12/00
CPC分类号： C10G9/18 , B01J4/004 , B01J8/0423 , B01J8/0438 , B01J8/0442 , B01J8/0453 , B01J8/0457 , B01J19/02 , B01J19/2485 , B01J2208/00106 , B01J2208/00309 , B01J2208/00327 , B01J2208/00495 , B01J2208/0053 , B01J2208/00911 , B01J2219/0004 , B01J2219/00117 , B01J2219/00121 , B01J2219/00139 , B01J2219/00155 , B01J2219/00159 , B01J2219/0281 , B01J2219/182 , B01J2219/185 , B01J2219/1923 , B01J2219/194 , B01J2219/1943 , B01J2219/1947 , C07C4/04 , C10G9/26 , F23L15/02 , Y02E20/348
摘要： The present disclosure relates to reactor components and their use, e.g., in regenerative reactors. A process and apparatus for utilizing different wetted areas along the flow path of a fluid in a pyrolysis reactor, e.g., a thermally regenerating reactor, such as a regenerative, reverse-flow reactor, is described.
摘要翻译：本公开涉及反应器组件及其在再生反应器中的用途。描述了在热解反应器（例如再生反应器，例如再生逆流反应器）中沿着流体的流动路径利用不同润湿区域的方法和装置。

3. 发明申请

US20150197696A1 Process and Apparatus for Converting Hydrocarbons 有权
标题翻译：用于转化烃类的方法和装置
公开(公告)号：US20150197696A1
公开(公告)日：2015-07-16
申请号：US13994229
申请日：2011-12-20
申请人： Paul F. Keusenkothen , Frank Hershkowitz
发明人： Paul F. Keusenkothen , Frank Hershkowitz
IPC分类号： C10G55/04 , B01D3/00 , C08F10/06 , C08F10/02 , C07C5/09 , B01J19/24
CPC分类号： C10G55/04 , B01D3/009 , B01J19/245 , B01J2219/24 , C07C2/76 , C08F10/02 , C08F10/06 , C10G9/002 , C10G9/005 , C10G9/007 , C10G9/16 , C10G9/18 , C10G9/26 , C07C11/24 , C07C11/04 , C07C11/06
摘要： An apparatus and process are provided for processing hydrocarbon feeds. The process enhances the conversion of hydrocarbon feeds into conversion products, such as ethylene and propylene. In particular, the present techniques utilize two high-severity pyrolysis reactors integrated with another reactor type to convert hydrocarbons to other petrochemical products. The pyrolysis reactors recycle a portion of one of the reactor products to at least one of the pyrolysis reactors to further enhance the process.
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，本技术利用与另一种反应器类型相结合的两种高等级热解反应器将碳氢化合物转化成其它石化产品。热解反应器将一部分反应器产物再循环至至少一个热解反应器，以进一步增强该方法。

4. 发明申请

US20140303416A1 Method and Apparatus for Converting Hydrocarbons Into Olefins 有权
标题翻译：将碳氢化合物转化成烯烃的方法和装置
公开(公告)号：US20140303416A1
公开(公告)日：2014-10-09
申请号：US13994220
申请日：2011-12-20
申请人： Paul F. Keusenkothen , Frank Hershkowitz
发明人： Paul F. Keusenkothen , Frank Hershkowitz
IPC分类号： C07C5/09 , C07C2/06 , C07C4/04
CPC分类号： C07C5/09 , C07C2/06 , C07C2/76 , C07C4/04 , C10G9/00 , C10G9/002 , C10G9/007 , C10G9/18 , C10G9/20 , C10G9/26 , C10G47/00 , C10G50/00 , C10G2300/4006 , C10G2300/4012 , C10G2300/42 , C10G2400/20 , C10G2400/22 , C10G2400/24 , C07C11/04 , C07C11/24
摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method may pass a pyrolysis feed to a thermal pyrolysis reactor and expose at least a portion of the pyrolysis feed to high-severity operating conditions in a thermal pyrolysis reactor, wherein the thermal pyrolysis reactor is operated at operating conditions that include pressure≧36 psig and provide a reactor product that has a C3+ to C2 unsaturate weight ratio≦0.5.
摘要翻译：提供了一种用于处理烃进料的装置和方法。该方法可以将热解原料通过热裂解反应器，并将热解原料的至少一部分暴露于高热解反应器中的高苛刻度的操作条件下，其中热裂解反应器在包括压力≥36psig 并提供具有C3 + C2不饱和重量比＆nlE; 0.5的反应器产物。

5. 发明申请

US20140296570A1 Hydrocarbon Conversion Process 有权
标题翻译：烃转化过程
公开(公告)号：US20140296570A1
公开(公告)日：2014-10-02
申请号：US13993194
申请日：2011-12-20
申请人： Paul F. Keusenkothen , Frank Hershkowitz
发明人： Paul F. Keusenkothen , Frank Hershkowitz
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。

6. 发明申请

US20140163287A1 Method and Apparatus for Managing Hydrogen Content Through The Conversion of Hydrocarbons Into Olefins 有权
标题翻译：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
申请人： Paul F. Keusenkothen , Frank Hershkowitz , Jason D. Davis , Gary D. Mohr
发明人： Paul F. Keusenkothen , Frank Hershkowitz , Jason D. Davis , Gary D. Mohr
IPC分类号： C07C4/04
CPC分类号： C07C4/04 , C07C11/04 , C07C11/24
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。

7. 发明授权

US08696888B2 Hydrocarbon resid processing 有权
标题翻译：烃渣处理
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。

8. 发明申请

US20130156656A1 Integrated Process For Steam Cracking 有权
标题翻译：蒸汽裂解综合工艺
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。

9. 发明授权

US08440070B2 Process and apparatus for converting high boiling point resid to light unsaturated hydrocarbons 有权
标题翻译：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
IPC分类号： C10G57/00 , C10G55/04
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。

10. 发明授权

US08083931B2 Upgrading of tar using POX/coker 有权
标题翻译：使用POX /焦化器升级焦油
公开(公告)号：US08083931B2
公开(公告)日：2011-12-27
申请号：US11881063
申请日：2007-07-25
申请人： James N. McCoy , Paul F. Keusenkothen , Alok Srivastava , James E Graham
发明人： James N. McCoy , Paul F. Keusenkothen , Alok Srivastava , James E Graham
IPC分类号： C10G57/00 , C10G27/04
CPC分类号： C10G51/023 , C10G55/04
摘要： The invention is directed to a process wherein a feedstock or stream comprising steam cracker tar is passed to a vacuum pipestill. A deasphalted cut of tar is obtained as an overhead (or sidestream) and a heavy tar asphaltenic product is obtained as bottoms. In preferred embodiments, at least a portion of the bottoms product is sent to a partial oxidation unit (POX) wherein syn gas may be obtained as a product, and/or at least a portion of the bottoms product is used to produce a light product stream in a coker unit, such as coker naphtha and/or or coker gas oil. In another preferred embodiment at least a portion of the overheads product is added to refinery fuel oil pools and in yet another preferred embodiment at least a portion of the overheads product is mixed with locally combusted materials to lower soot make. Two or more of the aforementioned preferred embodiments may be combined.
摘要翻译：本发明涉及一种方法，其中将包含蒸汽裂解焦油的原料或料流送入真空管道。作为塔顶（或侧流）获得焦油的脱沥青馏分，并且作为底部获得重质焦油沥青产物。在优选的实施方案中，将底部产物的至少一部分送至部分氧化单元（POX），其中可以获得产物的合成气，和/或至少部分底部产物用于生产轻质产物在焦化装置中，例如焦化石脑油和/或焦化瓦斯油。在另一个优选的实施方案中，将至少一部分塔顶馏出产物加入到炼油厂燃料油池中，在另一个优选的实施方案中，塔顶产物的至少一部分与局部燃烧的材料混合以降低烟灰。上述优选实施例中的两个或更多个可以组合。

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