发明名称 Process of producing a synthesis gas for methanol synthesis
摘要 In a reforming reactor operated with reactor outlet temperatures from 600 DEG to 1300 DEG C. and under a pressure from 10 to 100 bars, a methane-containing hydrocarbon gas is reacted with oxygen and water vapor. The reforming reactor is additionally fed with a high-hydrogen gas, which contains free hydrogen. The raw synthesis gas withdrawn from the reforming reactor is mainly composed of hydrogen, carbon monoxide and carbon dioxide. Without a removal of carbon dioxide from the raw synthesis gas, a synthesis gas is produced, which is suitable for the methanol synthesis and in which the concentrations of the components H2, CO and CO2 have a molar ratio (H2-CO2): (CO+CO2), called the stoichiometric number, from 1.97 to 2.2. In case of need, the stoichiometry number can be adjusted by adding hydrogen to the raw synthesis gas coming from the reforming reactor.
申请公布号 US5310506(A) 申请公布日期 1994.05.10
申请号 US19930120140 申请日期 1993.09.10
申请人 METALLGESELLSCHAFT AKTIENGESELLSCHAFT 发明人 SUPP, EMIL;MORGENROTH, RAINER
分类号 C01B3/38;C07C29/151;(IPC1-7):C01B3/38;C01B3/36 主分类号 C01B3/38
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