发明名称 Low pressure drop reforming exchanger
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.
申请公布号 US2003064011(A1) 申请公布日期 2003.04.03
申请号 US20010908307 申请日期 2001.07.18
申请人 BURLINGAME ROBERT;CZUPPON THOMAS A.;HACKEMESSER LARRY G. 发明人 BURLINGAME ROBERT;CZUPPON THOMAS A.;HACKEMESSER LARRY G.
分类号 B01J8/00;B01J8/02;B01J8/06;B01J19/30;B01J23/755;B01J35/02;C01B3/38;(IPC1-7):C01B3/26;B01L7/00;B01J35/04 主分类号 B01J8/00
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