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Autothermal reformer-reforming exchanger arrangement for hydrogen production

机译：用于制氢的自热重整器-重整交换器装置

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摘要

Low-energy, low-capital hydrogen production is disclosed. A reforming exchanger 14 is placed in parallel with an autothermal reformer (ATR) 10 to which are supplied a preheated steam-hydrocarbon mixture. An air-steam mixture is supplied to the burner/mixer of the ATR 10 to obtain a syngas effluent at 650°-1050° C. The effluent from the ATR is used to heat the reforming exchanger, and combined reformer effluent is shift converted and separated into a mixed gas stream and a hydrogen-rich product stream. High capital cost equipment such as steam-methane reformer and air separation plant are not required.

机译：公开了低能量，低资本氢生产。重整交换器14与自动热重整器（ATR）10平行放置，向其供应预热的蒸汽-烃混合物。将空气-蒸汽混合物供应到ATR 10的燃烧器/混合器，以获得650°-1050°C的合成气流出物。来自ATR的流出物用于加热重整交换器，合并的重整器流出物进行变换转换和分离成混合气流和富氢产物流。不需要高资本成本的设备，例如蒸汽甲烷重整器和空气分离装置。

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公开/公告号AU2004221826B2

专利类型
公开/公告日2009-12-17

原文格式PDF
申请/专利权人 KELLOGG BROWN & ROOT INC.;
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申请/专利号AU20040221826
发明设计人 JAMES HANLAN GOSNELL;AVINASH MALHOTRA;
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申请日2004-03-12
分类号C01B3/38;C01B32/50;B01J8/04;B01J8/06;C01B3/48;
国家 AU
入库时间 2022-08-21 18:41:59

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