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Afterburner methanol steam reformer/catalytic

Figure 7.9 100-Wei methanol steam reformer/catalytic afterburner [506]. Figure 7.9 100-Wei methanol steam reformer/catalytic afterburner [506].
Men et al. reported the operation of a small-scale bread-board methanol fuel processor composed of electrically heated reactors [15]. A methanol steam reformer, two-stage preferential oxidation reactors and a catalytic afterburner were switched in series. A fuel cell equipped with a reformate-tolerant membrane, which had a 20 W nominal power output, was connected to the fuel processor and operated for about 100 h. [Pg.937]

Shah and Besser presented results from their development work targeted at a 20 Wei methanol fuel processor-fuel cell system [66]. The layout of the system consisted of a methanol steam reformer, preferential oxidation, a catalytic afterburner and an evaporator. Vacuum packaging was the insulation strategy for the device, which is in line with other small-scale systems described above. A micro fixed-bed steam reformer coupled to a preferential oxidation reactor was then developed by the same group with a theoretical power output of 0.65 W. [Pg.939]

Figure 9.17 2.5-W methanol fuel processor developed by CASIO [568] right, catalytic afterburner (top), methanol steam reformer (centre) and preferential oxidation reactor (bottom). Figure 9.17 2.5-W methanol fuel processor developed by CASIO [568] right, catalytic afterburner (top), methanol steam reformer (centre) and preferential oxidation reactor (bottom).

See other pages where Afterburner methanol steam reformer/catalytic is mentioned: [Pg.343]    [Pg.344]    [Pg.192]    [Pg.305]    [Pg.305]    [Pg.308]    [Pg.309]    [Pg.312]   
See also in sourсe #XX -- [ Pg.246 ]




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Catalytic reformate

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Methanol steam reformer

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