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    Converting oxygenates to olefins over a catalyst comprising acidic molecular sieve of controlled carbon atom to acid site ratio
    25.
    发明授权
    Converting oxygenates to olefins over a catalyst comprising acidic molecular sieve of controlled carbon atom to acid site ratio 有权
    将含氧化合物转化为含有控制碳原子的酸性分子筛的催化剂与酸性位置比

    公开(公告)号：US07227048B2

    公开(公告)日：2007-06-05

    申请号：US10227907

    申请日：2002-08-26

    申请人： Paul N. Chisholm ,  Nicolas P. Coute ,  James R. Lattner ,  Teng Xu ,  Jeffrey S. Smith ,  Keith Holroyd Kuechler

    发明人： Paul N. Chisholm ,  Nicolas P. Coute ,  James R. Lattner ,  Teng Xu ,  Jeffrey S. Smith ,  Keith Holroyd Kuechler

    IPC分类号： C07C1/20

    CPC分类号： B01J38/12 ,  B01J29/85 ,  B01J29/90 ,  C07C1/20 ,  C07C2529/70 ,  C07C2529/85 ,  C10G3/49 ,  C10G3/62 ,  C10G2300/708 ,  C10G2400/20 ,  Y02P20/584 ,  Y02P30/20 ,  Y02P30/42 ,  C07C11/02

    摘要： The present invention provides a process for making an olefin product from an oxygenate-containing feedstock comprising:a) contacting the feedstock in a reaction zone with catalyst particles comprising a molecular sieve containing acid sites and having an average coke loading of 1 to 10 carbon atoms per acid site of said molecular sieve, under conditions effective to convert the feedstock into an olefin product stream and to provide unregenerated catalyst particles,b) removing a portion of said catalyst particles from said reaction zone and contacting said portion with a regeneration medium in a regeneration zone under conditions effective to obtain regenerated catalyst particles which have an average coke loading of no greater than 10 carbon atoms per acid site of said molecular sieve, andc) introducing said regenerated catalyst particles into said reaction zone to provide a catalyst mixture of unregenerated catalyst particles and regenerated catalyst particles, in an amount sufficient to provide an average coke loading on said catalyst mixture in an amount ranging from 1 to 10 carbon atoms per acid site of said molecular sieve.

    摘要翻译： 本发明提供了一种从含氧化合物原料制备烯烃产物的方法，包括：a）使反应区中的原料与包含含有酸性位点并具有1-10个碳原子的平均焦炭负载的分子筛的催化剂颗粒接触 在有效将原料转化为烯烃产物流并提供未再生催化剂颗粒的条件下，在所述分子筛的每个酸性位点处，b）从所述反应区除去一部分所述催化剂颗粒，并将所述部分与再生介质接触， 在有效获得在所述分子筛的每个酸性位点具有不大于10个碳原子的平均焦炭负载量的再生催化剂颗粒的条件下，c）将所述再生催化剂颗粒引入所述反应区以提供未再生的催化剂混合物 催化剂颗粒和再生催化剂颗粒，其量足够 以在所述催化剂混合物上提供在所述分子筛的每个酸性位置上具有1至10个碳原子的量的平均焦炭负载量。

    Organic compound conversion process
    30.
    发明授权
    Organic compound conversion process 有权
    有机化合物转化过程

    公开(公告)号：US08222468B2

    公开(公告)日：2012-07-17

    申请号：US12299276

    申请日：2006-05-08

    申请人： Michael C. Clark ,  Teng Xu ,  Matthew J. Vincent

    发明人： Michael C. Clark ,  Teng Xu ,  Matthew J. Vincent

    IPC分类号： C07C2/66 ,  C07C6/12

    CPC分类号： C07C2/12 ,  C07C2/66 ,  Y02P20/52 ,  C07C15/02 ,  C07C15/073 ,  C07C15/085

    摘要： The present invention provides a process for conversion of feedstock comprising organic compounds to desirable conversion product at organic compound conversion conditions in the presence of catalyst comprising an acidic, porous crystalline material and having a Proton Density Index of greater than 1.0, for example, from greater than 1.0 to about 2.0, e.g. from about 1.01 to about 1.85. The acidic, porous crystalline material of the catalyst may comprise a porous, crystalline material or molecular sieve having the structure of zeolite Beta, an MWW structure type material, e.g. MCM-22, MCM-36, MCM-49, MCM-56, or a mixture thereof.

    摘要翻译： 本发明提供了一种在有机化合物转化条件下在包含酸性多孔结晶材料并且具有大于1.0的质子密度指数（例如大于等于1.0）的催化剂存在下，将包含有机化合物的原料转化为所需转化产物的方法 大于1.0到大约2.0，例如 约1.01至约1.85。 催化剂的酸性多孔结晶材料可以包括具有沸石β结构的多孔结晶材料或分子筛，MWW结构类型材料例如沸石。 MCM-22，MCM-36，MCM-49，MCM-56或其混合物。