To reduce CO concentration while operating stably for a long term.
The fuel reforming system comprises providing at least a reforming reactor 1 and a CO selective oxidation reactor 2, wherein the reactor produces a reformed gas by reacting a raw fuel gas with steam and/or air under the coexistence of a reforming catalyst and the reactor produces a hydrogen rich gas converting into CO2 by selectively oxidizing CO in the reformed gas produced in the reforming reactor 1 under the coexistence of a CO selective oxidation catalyst. A steam condensing separation means 3 which condenses and separates steam contained in the reformed gas before feeding into the CO selective oxidation reactor 2 is provided between the reforming reactor 1 and the CO selective oxidation reactor 2. Steam is condensed and separated from the reforming gas which feeds into the CO selective oxidation reactor 2.
ECHIGO MITSUAKI
KAMIYA NORIHISA
TAKAMI SUSUMU
AZUMAGUCHI SEISAKU
HIRAI KAZUHIRO
JPH0640707A | 1994-02-15 | |||
JPH111301A | 1999-01-06 | |||
JP2003012302A | 2003-01-15 | |||
JPH08106913A | 1996-04-23 | |||
JPH1072202A | 1998-03-17 | |||
JPS5353596A | 1978-05-16 | |||
JPH10334935A | 1998-12-18 | |||
JPS6023652A | 1985-02-06 | |||
JPH10236802A | 1998-09-08 | |||
JP2000095506A | 2000-04-04 |
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