发明名称 Hydrogen production with reduced carbon dioxide generation and complete capture
摘要 The present invention is a method of reducing the carbon dioxide balance from a reformer furnace flue gas to the high pressure syngas exit water gas shift reaction unit. Introducing a heated gas mixture into at least one pre-reforming chamber. The heating being provided by indirect heat exchange with one or more of an SMR furnace flue gas or an SMR furnace syngas introducing the gas mixture into a standard H2 PSA unit, wherein the gas mixture is separated into a hydrogen enriched stream and a PSA tail gas stream; introducing the PSA tail gas stream into a CPU system, wherein the PSA tail gas stream is separated into a carbon dioxide enriched stream, a hydrogen rich stream, and a residual stream, and introducing the residual stream as fuel into the reformer furnace along with natural gas.
申请公布号 US8591769(B2) 申请公布日期 2013.11.26
申请号 US201113326983 申请日期 2011.12.15
申请人 VAUK DENNIS;GROVER BHADRA S.;AIR LIQUIDE LARGE INDUSTRIES U.S. LP;L'AIR LIQUIDE SOCIETE ANONYME POUR L'ETUDE ET L'EXPLOITATION DE PROCEDES GEORGES CLAUDE 发明人 VAUK DENNIS;GROVER BHADRA S.
分类号 C01B3/38;C01B3/26 主分类号 C01B3/38
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