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The model of TSOFC module consists of mixer, pre-reformer, internal reforming fuel cell group, afterburner and internal pre-heater components.
Both diluted hydrogen fuel and partially reformed methane streams with internal reforming are investigated.
Methane steam-reforming systems are typically operated at 700 to 800 °C; however, the internal reforming reaction in molten carbonate fuel cells occurs at the relatively low temperature between 580 and 650 °C at which the stack cell is operated.
The reformer was in-situ converting the methanol/steam feed to the required hydrogen (internal reforming concept) at 200 °C, which was readily oxidized at the anode electrodes.
A study of the kinetics of the methanol-steam reformation reaction within an idealized tube reactor and within a non-ideal internal reforming fuel cell (IRFC) was performed.
FCE's experience with internal reforming (indirect internal reforming and direct internal reforming catalysts) and fuel processing catalysts is discussed here.
In the SOFC module, internal reforming with anode gas recirculation is adopted.
A kW-class molten carbonate fuel cell with direct internal reforming is presented.
The system with internal reforming is less influenced by the constraint of the cell temperature difference.
Such a single cell configuration allows operation by gradual internal reforming of direct carbon-containing fuels.
High temperature operation of SOFCs can lead to the capability of internal reforming with fuel flexibility.
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