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    Low pressure drop reforming exchanger
    8.
    发明授权
    Low pressure drop reforming exchanger 有权
    低压降重整换热器

    公开(公告)号：US08216531B2

    公开(公告)日：2012-07-10

    申请号：US10905460

    申请日：2005-01-05

    申请人： Robert Burlingame ,  Thomas Czuppon ,  Larry G. Hackemesser

    发明人： Robert Burlingame ,  Thomas Czuppon ,  Larry G. Hackemesser

    IPC分类号： B01J8/00

    CPC分类号： B01J8/0292 ,  B01J8/008 ,  B01J8/067 ,  B01J19/30 ,  B01J23/755 ,  B01J35/026 ,  B01J2208/00221 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/30223 ,  B01J2219/30242 ,  B01J2219/32296 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/0844 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/82 ,  Y02P20/52

    摘要： Disclosed are a syngas production process and a reforming exchanger 100. The process involves passing a first portion of hydrocarbon feed mixed with steam and oxidant through an autothermal catalytic steam reforming zone to form a first reformed gas of reduced hydrocarbon content, passing a second portion of the hydrocarbon feed mixed with steam through an endothermic catalytic steam reforming zone to form a second reformed gas of reduced hydrocarbon content, and mixing the first and second reformed gases and passing the resulting gas mixture through a heat exchange zone for cooling the gas mixture and thereby supplying heat to the endothermic catalytic steam reforming zone. The endothermic catalytic steam reforming zone and the heat exchange zone are respectively disposed tube side and shell side within a shell-and-tube reforming exchanger 100. The reforming exchanger 100 comprises a plurality of tubes 118 packed with low pressure drop catalyst-bearing monolithic structures 200 wherein an inside diameter of the tubes 118 is less than 4 times a maximum edge dimension of the catalyst structures 200.

    摘要翻译： 公开了合成气生产方法和重整交换器100.该方法包括将与蒸汽和氧化剂混合的烃进料的第一部分通过自热催化蒸汽重整区，以形成具有降低的烃含量的第一重整气体，将第二部分 所述烃进料通过吸热催化蒸汽重整区与蒸汽混合以形成具有降低的烃含量的第二重整气体，并且混合第一和第二重整气体并使得到的气体混合物通过用于冷却气体混合物的热交换区 向吸热催化蒸汽重整区供热。 吸热催化蒸汽重整区和热交换区分别设置在管 - 管重整交换器100内的管侧和壳侧。重整交换器100包括多个管118，管118装有低压降催化剂承载整体结构 200，其中管118的内径小于催化剂结构200的最大边缘尺寸的4倍。

    Low pressure drop reforming exchanger
    10.
    发明授权
    Low pressure drop reforming exchanger 有权
    低压降重整换热器

    公开(公告)号：US06855272B2

    公开(公告)日：2005-02-15

    申请号：US09908307

    申请日：2001-07-18

    申请人： Robert Burlingame ,  Thomas A. Czuppon ,  Larry G. Hackemesser

    发明人： Robert Burlingame ,  Thomas A. Czuppon ,  Larry G. Hackemesser

    IPC分类号： B01J8/00 ,  B01J8/02 ,  B01J8/06 ,  B01J19/30 ,  B01J23/755 ,  B01J35/02 ,  C01B3/38

    CPC分类号： B01J8/0292 ,  B01J8/008 ,  B01J8/067 ,  B01J19/30 ,  B01J23/755 ,  B01J35/026 ,  B01J2208/00221 ,  B01J2208/00309 ,  B01J2208/00495 ,  B01J2208/0053 ,  B01J2219/30223 ,  B01J2219/30242 ,  B01J2219/32296 ,  C01B3/382 ,  C01B3/384 ,  C01B2203/0844 ,  C01B2203/141 ,  C01B2203/142 ,  C01B2203/82 ,  Y02P20/52

    摘要： Syngas production process and reforming exchanger. The process involves passing a first portion of hydrocarbon feed mixed with steam and oxidant through an autothermal catalytic steam reforming zone to form a first reformed gas of reduced hydrocarbon content, passing a second portion of the hydrocarbon feed mixed with steam through an endothermic catalytic steam reforming zone to form a second reformed gas of reduced hydrocarbon content, and mixing the first and second reformed gases and passing the resulting gas mixture through a heat exchange zone for cooling the gas mixture and thereby supplying heat to the endothermic catalytic steam reforming zone. The endothermic catalytic steam reforming zone and the heat exchange zone are respectively disposed tube side and shell side within a shell-and-tube reforming exchanger. The reforming exchanger comprises a plurality of tubes packed with low pressure drop catalyst-bearing monolithic structures wherein an inside diameter of the tubes is less than 4 times a maximum edge dimension of the catalyst structures.

    摘要翻译： 合成气生产过程和重整换热器。 该方法包括使与蒸汽和氧化剂混合的烃进料的第一部分通过自热催化蒸汽重整区，以形成具有降低的烃含量的第一重整气体，使与蒸汽混合的烃进料的第二部分通过吸热催化蒸汽重整 形成还原烃含量的第二重整气体，并混合第一和第二重整气体，并使得到的气体混合物通过热交换区，用于冷却气体混合物，从而向吸热催化蒸汽重整区供热。 吸热催化蒸汽重整区和热交换区分别在管 - 管重整交换器内设置管侧和壳侧。 重整交换器包括多个管，其填充有低压降催化剂承载整体结构，其中管的内径小于催化剂结构的最大边缘尺寸的4倍。