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    Process for the production of mixed alcohols
    71.
    发明申请
    Process for the production of mixed alcohols 有权
    混合醇生产工艺

    公开(公告)号：US20070259972A1

    公开(公告)日：2007-11-08

    申请号：US11716274

    申请日：2007-03-09

    申请人： James R. Lattner ,  Michel Molinier ,  Kun Wang

    发明人： James R. Lattner ,  Michel Molinier ,  Kun Wang

    IPC分类号： C07C27/00

    CPC分类号： C07C29/1518 ,  C07C1/20 ,  C07C1/24 ,  Y02P30/42 ,  C07C11/02 ,  C07C31/04 ,  C07C31/08

    摘要： The present invention relates to processes for forming mixed alcohols containing methanol and ethanol. The mixed alcohol can then be used as a feedstock for an oxygenate-to-olefin reaction system for conversion thereof to ethylene, propylene, and the like. In addition, the olefins produced by the oxygenate-to-olefin reaction can then be used as monomers for a polymerization of olefin-containing polymers and/or oligomers.

    摘要翻译： 本发明涉及形成含有甲醇和乙醇的混合醇的方法。 然后可以将混合的醇用作用于将其转化成乙烯，丙烯等的含氧化合物至烯烃反应体系的原料。 此外，通过含氧化合物与烯烃反应产生的烯烃可以用作用于烯烃聚合物和/或低聚物聚合的单体。

    Fluid bed oxygenates to olefins reactor apparatus and process of controlling same
    72.
    发明授权
    Fluid bed oxygenates to olefins reactor apparatus and process of controlling same 有权
    流化床含氧物到烯烃反应器装置及其控制过程

    公开(公告)号：US07273960B2

    公开(公告)日：2007-09-25

    申请号：US10280817

    申请日：2002-10-25

    申请人： James R. Lattner

    发明人： James R. Lattner

    IPC分类号： C07C1/20

    CPC分类号： C10G11/187 ,  B01J29/90 ,  B01J38/30 ,  C07C1/20 ,  C10G3/49 ,  C10G3/62 ,  C10G9/007 ,  C10G11/16 ,  C10G11/18 ,  C10G11/182 ,  C10G2300/4006 ,  C10G2300/4018 ,  C10G2300/708 ,  C10G2400/20 ,  Y02P20/584 ,  Y02P30/20 ,  C07C11/02

    摘要： A reactor apparatus and related method for controlling at least one process variable in a circulating fluid bed oxygenates to olefins reactor system comprising a riser are provided. The process variable is selected from at least one of (i) space velocity, (ii) average reaction temperature, (iii) conversion of reactant, and (iv) average coke level on catalyst. Typically, a corresponding set point for at least one process variable is selected from (1) reactant feed rate, (2) feed enthalpy, (3) reactor temperature-related function, e.g., mid-temperature or rate of temperature rise along a portion of the reactor, and (4) catalyst hold-up in the riser of the reactor. A corresponding manipulated variable is selected from (a) feed flow control valve(s), (b) feed preheat rate, (c) activity of the catalyst in the reactor, and (d) amount of catalyst in the reaction zone. The combination of measured and manipulated variables described here allows for smooth, stable control of the reactor at the optimum performance level.

    摘要翻译： 提供了一种用于控制循环流化床中至少一个工艺变量的反应器装置和相关方法，包含提升管的含氧化合物至烯烃反应器系统。 过程变量选自（i）空间速度，（ii）平均反应温度，（iii）反应物的转化率和（iv）催化剂上的平均焦炭水平中的至少一个。 通常，从（1）反应物进料速率，（2）进料焓，（3）反应器温度相关函数，例如沿着一部分的中温或温度升高速率选择至少一个过程变量的相应设定点 的反应器，和（4）催化剂滞留在反应器的提升管中。 从（a）进料流量控制阀，（b）进料预热速率，（c）反应器中催化剂的活性和（d）反应区中的催化剂的量选择相应的操作变量。 这里描述的测量和操作变量的组合允许在最佳性能水平下平稳，稳定地控制反应器。

    Methanol manufacture using pressure swing reforming
    75.
    发明授权
    Methanol manufacture using pressure swing reforming 有权
    使用压力挥发重整的甲醇制造

    公开(公告)号：US07183328B2

    公开(公告)日：2007-02-27

    申请号：US10738782

    申请日：2003-12-17

    申请人： Frank Hershkowitz ,  James R. Lattner

    发明人： Frank Hershkowitz ,  James R. Lattner

    IPC分类号： C07C27/00 ,  C07C1/00

    CPC分类号： C07C29/1518 ,  Y02P30/42 ,  C07C31/04 ,  C07C31/08 ,  C07C31/10 ,  C07C31/02

    摘要： A process for producing methanol is described in which a hydrocarbon is steam reformed in a reforming zone, and during the reforming stage, of a cyclic steam reformer having a reforming stage and a regeneration stage, the steam reforming being conducted under conditions effective to produce a first effluent stream containing synthesis gas. A fuel and an oxygen-containing gas are combusted in the regeneration stage of the reformer so as to reheat the reforming zone to a temperature sufficient for the reforming stage and generate a flue gas. At least part of the first effluent stream is contacted with a methanol synthesis catalyst under conditions effective to convert synthesis gas to methanol and form a methanol-containing stream and a tail gas stream comprising unreacted carbon monoxide and hydrogen. Hydrogen is separated from at least one of the first effluent stream and the tail gas stream and at least part of the hydrogen is recycled as part of the fuel for the regeneration stage of the cyclic steam reformer.

    摘要翻译： 描述了一种生产甲醇的方法，其中烃在重整区中进行蒸汽重整，并且在重整阶段期间，在具有重整阶段和再生阶段的循环蒸汽重整器中，蒸汽重整在有效产生 含有合成气的第一流出物流。 燃料和含氧气体在重整器的再生阶段中燃烧，以便将重整区重新加热到足以用于重整阶段的温度并产生烟道气。 在有效地将合成气转化成甲醇并形成含甲醇流和包含未反应的一氧化碳和氢气的尾气流的条件下，将至少部分第一流出物流与甲醇合成催化剂接触。 氢气与第一流出物流和尾气流中的至少一个分离，并且至少部分氢气作为用于循环蒸汽重整器的再生阶段的燃料的一部分被再循环。

    Multiple riser reactor
    76.
    发明授权
    Multiple riser reactor 有权
    多立管反应堆

    公开(公告)号：US07102050B1

    公开(公告)日：2006-09-05

    申请号：US09564613

    申请日：2000-05-04

    申请人： James R. Lattner ,  Jeffrey S. Smith ,  Nicolas P. Coute ,  Keith H. Kuechler

    发明人： James R. Lattner ,  Jeffrey S. Smith ,  Nicolas P. Coute ,  Keith H. Kuechler

    IPC分类号： C07C1/00

    CPC分类号： B01J8/26 ,  B01J8/0055 ,  B01J8/1845 ,  B01J8/1872 ,  C10G3/49 ,  C10G3/62 ,  C10G11/18 ,  C10G2300/4093 ,  C10G2400/20 ,  Y10S585/921 ,  Y10S585/922 ,  Y10S585/923 ,  Y10S585/926

    摘要： The present invention is directed to a hydrocarbon conversion apparatus. The apparatus comprises the following: a plurality of riser reactors, each of the riser reactors having a first end into which a catalyst can be fed and a second end through which the catalyst can exit the riser reactor; a separation zone into which the second ends of the riser reactors extend, the separation zone being provided to separate the catalyst from products of a reaction conducted in the hydrocarbon conversion apparatus; and at least one catalyst return in fluid communication with the separation zone and the first ends of the riser reactors, the catalyst return being provided to transfer the catalyst from the separation zone to the first ends of the riser reactors.

    摘要翻译： 本发明涉及烃转化装置。 该设备包括以下：多个提升管反应器，每个提升管反应器具有第一端，催化剂可以进入该第一端，催化剂可以通过该第二端离开提升管反应器; 分离区，其中提升管反应器的第二端延伸到其中，分离区被提供以将催化剂与在烃转化装置中进行的反应的产物分离; 并且至少一个催化剂返回与分离区和提升管反应器的第一端流体连通，提供催化剂返回以将催化剂从分离区转移到提升管反应器的第一端。