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    Method and Apparatus for Converting Hydrocarbons Into Olefins Using Hydroprocessing and Thermal Pyrolysis
    72.
    发明申请
    Method and Apparatus for Converting Hydrocarbons Into Olefins Using Hydroprocessing and Thermal Pyrolysis 有权
    使用加氢处理和热解法将碳氢化合物转化成烯烃的方法和装置

    公开(公告)号：US20150166430A1

    公开(公告)日：2015-06-18

    申请号：US13994476

    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： C07C4/04 ,  C08F110/02 ,  B01J19/24 ,  C10G47/02 ,  C07C5/09

    CPC分类号： C07C4/04 ,  B01J19/245 ,  B01J2219/24 ,  C07C5/09 ,  C08F110/02 ,  C10G47/02 ,  C07C11/04 ,  C07C11/24

    摘要： An apparatus and method are provided for processing hydrocarbon feeds. The method may contact hydrogen (H2) and a hydrocarbon feed containing ≧10 wt % resid in the hydrocarbon feed with a catalyst to form a hydroprocessed product. Then, a pyrolysis feed derived from the hydroprocessed product is exposed at high-severity thermal pyrolysis operating conditions to produce a reactor product that comprises ethylene and acetylene. Further, at least a portion of the hydrogen (H2) may be separated from the reactor product, wherein the hydrogen (H2) contacting the catalyst includes at least a portion of the separated hydrogen (H2).

    摘要翻译： 提供了一种用于处理烃进料的装置和方法。 该方法可以与催化剂接触氢（H 2）和含有≥10重量％的烃进料的烃进料以形成加氢产物。 然后，来自加氢处理产物的热解原料在高严重性热裂解操作条件下暴露以产生包含乙烯和乙炔的反应器产物。 此外，氢（H 2）的至少一部分可以与反应器产物分离，其中与催化剂接触的氢（H 2）包括分离的氢（H 2）的至少一部分。

    Hydrocarbon Pyrolysis Method
    76.
    发明申请
    Hydrocarbon Pyrolysis Method 有权
    烃热解法

    公开(公告)号：US20130211165A1

    公开(公告)日：2013-08-15

    申请号：US13735365

    申请日：2013-01-07

    申请人： James R. Lattner ,  Paul F. Keusenkothen ,  Frank Hershkowitz

    发明人： James R. Lattner ,  Paul F. Keusenkothen ,  Frank Hershkowitz

    IPC分类号： C07C5/327 ,  B01J8/02

    CPC分类号： C07C5/327 ,  B01J8/0292 ,  C07C2/78 ,  C07C11/24 ,  C07C11/04

    摘要： Disclosed is a pyrolysis reaction process. The process can be advantageously accomplished using a pyrolysis reactor that has a primary reaction zone comprised of bed packing having multiple passages through the bed packing and a secondary reaction zone having an open flow arrangement. The process includes a step of injecting a pyrolysis feed comprising a first hydrocarbon into the primary reaction zone to produce a primary pyrolysis product containing unsaturated hydrocarbon. A reactive feed comprising a second hydrocarbon is injected into the secondary reaction zone to mix with the primary pyrolysis product and produce a secondary pyrolysis product.

    摘要翻译： 披露了热解反应过程。 该方法可以有利地使用热解反应器来实现，该热解反应器具有由具有穿过床填料的多个通道的床填料和具有开放流动排列的次级反应区组成的初级反应区。 该方法包括将包含第一烃的热解原料注入初级反应区以产生含有不饱和烃的初级热解产物的步骤。 将包含第二烃的反应性进料注入到次级反应区中以与初级热解产物混合并产生二级热解产物。

    Porous Pyrolysis Reactor Materials And Methods
    78.
    发明申请
    Porous Pyrolysis Reactor Materials And Methods 有权
    多孔热解反应堆材料与方法

    公开(公告)号：US20110120853A1

    公开(公告)日：2011-05-26

    申请号：US12623046

    申请日：2009-11-20

    申请人： ChangMin Chun ,  Frank Hershkowitz ,  Paul F. Keusenkothen ,  Shiun Ling ,  Gary David Mohr

    发明人： ChangMin Chun ,  Frank Hershkowitz ,  Paul F. Keusenkothen ,  Shiun Ling ,  Gary David Mohr

    IPC分类号： C10G9/00 ,  C10B29/00 ,  C10B57/16

    CPC分类号： C10G9/203 ,  C10G9/16 ,  C10G2300/4075

    摘要： In one aspect, the invention includes a reactor apparatus for pyrolyzing a hydrocarbon feedstock, said apparatus including: a reactor component comprising a refractory material in oxide form, the refractory material having a melting point of no less than 2060° C. and which remains in oxide form when exposed to a gas having carbon partial pressure of 10−22 bar and oxygen partial pressure of 10−10 bar, at a temperature of 1200° C.; wherein said refractory material has no less than 4 vol % formed porosity, measured at 20° C., based upon the bulk volume of said refractory material. In another embodiment, the refractory material has total porosity in the range of from 4 to 60 vol %.

    摘要翻译： 在一个方面，本发明包括用于热解烃原料的反应器装置，所述装置包括：反应器组件，其包含氧化物形式的耐火材料，耐火材料的熔点不低于2060℃，并保持在 在1200℃的温度下暴露于碳分压为10-22巴，氧气分压为10-10巴的气体时，氧化物形式。 其中所述耐火材料具有基于所述耐火材料的体积体积在20℃下测量的不少于4体积％的孔隙率。 在另一个实施方案中，耐火材料具有4至60体积％的总孔隙率。

    Process and apparatus for using steam cracked tar as steam cracker feed
    80.
    发明授权
    Process and apparatus for using steam cracked tar as steam cracker feed 有权
    使用蒸汽裂解焦油作为蒸汽裂化器进料的方法和设备

    公开(公告)号：US07815791B2

    公开(公告)日：2010-10-19

    申请号：US12112704

    申请日：2008-04-30

    申请人： Paul F. Keusenkothen

    发明人： Paul F. Keusenkothen

    IPC分类号： C10C1/20

    CPC分类号： C10G69/06

    摘要： A process and apparatus are provided for steam cracking heavy feeds, including steam cracked tars. The invention heats a steam cracked tar feed to provide a depolymerized steam cracked tar containing lower boiling molecules than the steam cracked tar feed, hydrogenates the depolymerized steam cracked tar using a hydrogenating catalyst, e.g., a downward flow fixed bed hydrotreater, to provide a hydrogenated steam cracked tar. At least a portion of the hydrogenated steam cracked tar is steam cracked in a steam cracking furnace comprising a convection zone and a radiant zone.

    摘要翻译： 提供了一种用于蒸汽破裂重料，包括蒸汽裂纹焦油的方法和装置。 本发明加热蒸汽裂解的焦油进料，以提供含有比蒸汽裂解的焦油进料更低沸点分子的解聚的蒸汽裂解焦油，使用氢化催化剂（例如向下流动的固定床加氢处理器）氢化解聚的蒸汽裂化焦油，以提供氢化 蒸汽裂解焦油。 氢化蒸汽裂解焦油的至少一部分在包括对流区和辐射区的蒸汽裂解炉中蒸汽裂解。