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25 条记录 (耗时 0.068 秒)

    Process for the production of xylenes and light olefins
    11.
    发明授权
    Process for the production of xylenes and light olefins 有权
    生产二甲苯和轻质烯烃的方法

    公开(公告)号：US09181147B2

    公开(公告)日：2015-11-10

    申请号：US13465733

    申请日：2012-05-07

    申请人： Larry L. Iaccino ,  S. Mark Davis ,  John D. Y. Ou ,  Xiaobo Zheng

    发明人： Larry L. Iaccino ,  S. Mark Davis ,  John D. Y. Ou ,  Xiaobo Zheng

    IPC分类号： C07C1/24 ,  C07C2/86 ,  C10G29/20 ,  C10G35/00 ,  C10G57/00 ,  C10G9/00 ,  C10G9/36 ,  C10G11/00

    CPC分类号： C07C2/864 ,  C10G9/005 ,  C10G9/36 ,  C10G11/00 ,  C10G29/205 ,  C10G35/00 ,  C10G57/005 ,  C10G2300/1092 ,  C10G2300/1096 ,  C10G2400/30 ,  C07C15/08

    摘要： In a hydrocarbon upgrading process, a hydrocarbon feed is treated in at least one of a steam cracker, catalytic cracker, coker, hydrocracker, and reformer under suitable conditions to produce a first stream comprising olefinic and aromatic hydrocarbons. A second stream composed mainly of C4+ olefinic and aromatic hydrocarbons is recovered from the first stream and is fed together with a methylating agent to a reaction zone containing a catalyst under reaction conditions including a temperature of about 450° C. to about 700° C., such that aromatics components in the second stream undergo dealkylation, transalkylation and/or methylation and aliphatic components undergo cracking and aromatization to produce a third stream having an increased xylene content compared with said second stream and a C3− olefin by-product. The C3− olefin by-product is recovered and para-xylene is removed from at least part of said third stream.

    摘要翻译： 在烃改质方法中，在合适条件下，在蒸汽裂化器，催化裂化器，焦化器，加氢裂化器和重整器中的至少一种中处理烃进料以产生包含烯烃和芳族烃的第一流。 从第一流回收主要由C4 +烯烃和芳烃组成的第二料流，并在包括约450℃至约700℃的温度的反应条件下与甲基化剂一起加入含有催化剂的反应区。 使得第二流中的芳烃组分经历脱烷基化，烷基转移和/或甲基化，并且脂族组分经历裂化和芳构化以产生与所述第二料流和C3-烯烃副产物相比具有增加的二甲苯含量的第三料流。 回收C3-烯烃副产物，并从至少部分所述第三料流中除去对二甲苯。

    Mercury removal by dispersed-metal adsorbents
    13.
    发明授权
    Mercury removal by dispersed-metal adsorbents 失效
    通过分散金属吸附剂去除汞

    公开(公告)号：US5463167A

    公开(公告)日：1995-10-31

    申请号：US372695

    申请日：1995-01-13

    申请人： John D. Y. Ou

    发明人： John D. Y. Ou

    IPC分类号： C10G25/00 ,  C07C7/12 ,  C10G17/00

    CPC分类号： C10G25/003

    摘要： A method of removing contaminants from a hydrocarbon stream which involves contacting the hydrocarbon stream containing a heavy-metal contaminant with a porous material under conditions suitable for adsorption of the contaminant by the porous material. A process for preparing an adsorbent which involves forming a mixture of metal oxide powder and support powder, shaping the mixture into an aggregate, and reducing the aggregate to transform the metal oxide to the metallic state.

    摘要翻译： 从烃流中除去污染物的方法，其包括在适于通过多孔材料吸附污染物的条件下使含有重金属污染物的烃流与多孔材料接触。 一种制备吸附剂的方法，其包括形成金属氧化物粉末和载体粉末的混合物，将混合物成形为聚集体，并还原骨料以将金属氧化物转化为金属状态。

    Removal of organochlorides from hydrocarbon feed streams
    14.
    发明授权
    Removal of organochlorides from hydrocarbon feed streams 失效
    从油料进料流中去除有机氯化物

    公开(公告)号：US5107061A

    公开(公告)日：1992-04-21

    申请号：US505816

    申请日：1990-04-06

    申请人： John D. Y. Ou ,  Daniel D. Rosenfeld

    发明人： John D. Y. Ou ,  Daniel D. Rosenfeld

    IPC分类号： C10G25/02 ,  A62D3/00 ,  A62D3/34 ,  A62D101/22 ,  C07C7/13 ,  C07C7/148 ,  C10G25/03 ,  C10G25/05

    CPC分类号： A62D3/34 ,  C07C7/148 ,  C10G25/05 ,  A62D2101/22

    摘要： The present invention is directed to the removal of organochlorides from hydrocarbon streams using highly crystalline molecular sieve material, such as zeolites, and particularly zeolite X in a sodium form, and the removal of organochlorides from hydrocarbon streams containing olefinic compounds using such molecular sieves in combination with alumina for the purpose of effecting a decomposition of the organochloride into a corresponding unsaturated hydrocarbon molecule and a molecule of hydrocarbon chloride wherein the hydrocarbon chloride is removed from the hydrocarbon stream by being adsorbed onto the adsorbent of the highly crystalline molecular sieve used alone, or in combination with alumina in those instances where olefinic compounds are present in the hydrocarbon stream, so that the unsaturated hydrocarbon molecule may be recovered from the resultant hydrocarbon stream containing a reduced amount of organochlorides.

    摘要翻译： 本发明涉及使用高结晶分子筛材料（例如沸石，特别是钠形式的沸石X）从烃流中除去有机氯化物，并且使用这种分子筛组合从含有烯烃化合物的烃流中除去有机氯化物 氧化铝用于将有机氯化物分解成相应的不饱和烃分子和烃氯化物的分子，其中通过吸附到单独使用的高结晶分子筛的吸附剂上将烃氯化物从烃流中除去，或 在烃流中存在烯烃化合物的情况下与氧化铝组合，从而可以从含有减少量的有机氯化物的所得烃流中回收不饱和烃分子。

    Process and apparatus for upgrading steam cracker tar-containing effluent using steam
    15.
    发明授权
    Process and apparatus for upgrading steam cracker tar-containing effluent using steam 有权
    使用蒸汽升级蒸汽裂解炉含焦油流出物的工艺和设备

    公开(公告)号：US08105479B2

    公开(公告)日：2012-01-31

    申请号：US12486813

    申请日：2009-06-18

    申请人： John D. Y. Ou ,  Glenn A. Heeter

    发明人： John D. Y. Ou ,  Glenn A. Heeter

    IPC分类号： C10C3/02

    CPC分类号： C10G9/00 ,  C10C1/00 ,  C10G2300/206 ,  C10G2300/301 ,  C10G2300/807 ,  C10G2400/20

    摘要： A process and apparatus are provided for the present invention relates to a process for upgrading tar-containing effluent from a steam cracker furnace that comprises: a) contacting a steam cracker tar-containing effluent with steam and for a time, sufficient to convert at least a portion of the steam cracker tar to a mixture comprising lower boiling molecules and the steam cracker tar-containing effluent; and b) separating the mixture from step a) into i) at least one tar-lean product; and ii) a tar-rich product having a final boiling above the final boiling point of the at least one tar-lean product. Step a) can includes at least one of: 1) contacting said steam cracker tar-containing effluent with steam added to the effluent in a transfer line downstream of a steam cracker furnace comprising a quench inlet, with the steam added through or downstream of the quench inlet; 2) contacting the steam cracker tar-containing effluent with steam under heat soaking conditions in a heat soaking vessel to which the steam is added; and 3) contacting the steam cracker tar-containing effluent with steam under visbreaking conditions in a visbreaker. The steam treated tar can be separated into higher value gas oil, fuel oil and tar streams.

    摘要翻译： 提供了一种方法和装置，本发明涉及一种用于升级来自蒸汽裂化炉的含焦油流出物的方法，该方法包括：a）使蒸汽裂解焦油含有流出物与蒸汽接触一段时间，足以至少转化 蒸汽裂化器焦油的一部分到包含较低沸点分子的混合物和含蒸汽裂解物焦油的流出物; 和b）将混合物与步骤a）分离成i）至少一种焦油产品; 和ii）具有高于至少一种焦油产品的最终沸点的最终沸点的焦油富产品。 步骤a）可以包括以下中的至少一个：1）将所述含蒸汽裂解焦油的流出物与蒸汽加料到流出物中的蒸汽接触，所述蒸汽在包含骤冷入口的蒸汽裂解炉的下游的输送管线中， 淬火入口 2）在加热浸泡条件下将含蒸汽裂解焦油的流出物与蒸汽接触，在加热蒸汽的加热容器中; 和3）在减粘裂化条件下将含蒸汽裂解焦油的流出物与蒸汽接触。 蒸汽处理的焦油可以分成更高价值的瓦斯油，燃料油和焦油流。

    Catalyst selectivation
    17.
    发明授权
    Catalyst selectivation 失效
    催化剂选择

    公开(公告)号：US06613708B1

    公开(公告)日：2003-09-02

    申请号：US09327241

    申请日：1999-06-07

    申请人： John D. Y. Ou ,  Youchang Xie ,  Biying Zhao ,  Xiangyun Long ,  Xiawan Yang ,  Lili Guan

    发明人： John D. Y. Ou ,  Youchang Xie ,  Biying Zhao ,  Xiangyun Long ,  Xiawan Yang ,  Lili Guan

    IPC分类号： B01J2904

    CPC分类号： B01J29/405 ,  B01J29/061 ,  B01J37/0203 ,  B01J37/086 ,  B01J2229/12 ,  B01J2229/34

    摘要： It has been discovered that catalysts may be modified by depositing an agent derivative from an agent such as an organometallic compound upon them. Such a modification gives a catalyst useful in increased selectivity to para-substituted alkyl benzenes, such as para-xylene (PX), through reacting an aromatic compound such as toluene and/or benzene with a methylating agent from hydrogen and carbon monoxide and/or carbon dioxide and/or methanol. Using these selectivated catalysts, para-substituted alkyl benzenes can be recovered in a selectivity of 80% or greater, significantly better than the equilibrium concentration of 24%.

    摘要翻译： 已经发现，可以通过从其中的试剂如有机金属化合物沉积试剂衍生物来改变催化剂。 通过使芳族化合物如甲苯和/或苯与甲基化剂从氢气和一氧化碳和/或其混合物反应，这种改性可提供对对取代的烷基苯（如对二甲苯（PX））增加选择性的催化剂。 二氧化碳和/或甲醇。 使用这些选择性催化剂，可以以80％或更高的选择性回收对位取代的烷基苯，显着优于24％的平衡浓度。

    Removal of nitrogenous components of a hydrocarbon feedstream
    19.
    发明授权
    Removal of nitrogenous components of a hydrocarbon feedstream 失效
    去除碳氢化合物原料流中的含氮组分

    公开(公告)号：US5120881A

    公开(公告)日：1992-06-09

    申请号：US502214

    申请日：1990-03-30

    申请人： Daniel D. Rosenfeld ,  John D. Y. Ou

    发明人： Daniel D. Rosenfeld ,  John D. Y. Ou

    IPC分类号： C07B63/00 ,  C07C7/13 ,  C07C41/06 ,  C07C41/42 ,  C07C43/04

    CPC分类号： C07C41/42 ,  C07C41/06 ,  C07C7/13

    摘要： A catalytic reaction process which involves exposing a hydrocarbon feed including nitrogenous contaminants as well as dialkyl sulfides to a material capable of adsorbing the nitrogenous contaminants as well as dialkyl sulfides from the feed before introducing the stream substantially devoid of nitrogenous contaminants and dimethyl sulfide into a feed zone of a reactor; contacting the hydrocarbon stream with a catalyst material in the reaction zone; and catalytically reacting the hydrocarbon stream under conditions which favor forming a reaction product and inhibiting reaction of nitrogenous contaminants and dimethyl sulfide with the catalyst material.

    摘要翻译： 一种催化反应方法，其包括在将基本上没有含氮污染物和二甲基硫化物的料流引入进料之前将包括含氮污染物和二烷基硫化物的烃进料暴露于能够从进料中吸附含氮污染物以及二烷基硫化物的材料 反应堆区; 使烃流与反应区中的催化剂材料接触; 并在有利于形成反应产物并抑制含氮污染物和二甲基硫醚与催化剂材料的反应的条件下催化反应烃流。