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    Porous pyrolysis reactor materials and methods
    2.
    发明授权
    Porous pyrolysis reactor materials and methods 有权
    多孔热解反应器的材料及方法

    公开(公告)号：US08932534B2

    公开(公告)日：2015-01-13

    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： B01J19/00 ,  C10G9/20 ,  C10G9/16 ,  B01J19/24 ,  C10G9/00 ,  C10G11/00

    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。

    Porous Pyrolysis Reactor Materials And Methods
    6.
    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。

    Preparation of high silica zeolites bound by zeolite and use thereof
    8.
    发明授权
    Preparation of high silica zeolites bound by zeolite and use thereof 有权

    公开(公告)号：US06645370B2

    公开(公告)日：2003-11-11

    申请号：US10315353

    申请日：2002-12-10

    申请人： Johannes P. Verduijn ,  Gary David Mohr

    发明人： Johannes P. Verduijn ,  Gary David Mohr

    IPC分类号： C10G1105

    CPC分类号： C01B39/026 ,  B01J29/40 ,  B01J37/0009 ,  B01J2229/42 ,  Y10S423/22

    摘要： This invention relates to a process for producing zeolite-bound high silica zeolites and the use of the zeolite-bound high silica zeolite produced by the process for hydrocarbon conversion. The process is carried out by forming an extrudable paste comprising a mixture of high silica zeolite in the hydrogen form, water, silica, and optionally an extrusion aid, extruding the extrudable paste to form silica-bound high silica zeolite extrudates, and then converting the silica of the binder to a zeolite binder. The zeolite-bound high silica zeolite produced by the process comprises high silica zeolite crystals that are bound together by zeolite binder crystals. The zeolite-bound high silica zeolite finds particular application in hydrocarbon conversion processes, e.g., catalytic cracking, alkylation, disproportionation of toluene, isomerization, and transalkylation reactions.