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The autothermal reforming performance of the reformer for different fuels was evaluated with regard to hydrogen selectivity, COx selectivity, and energy conversion efficiency.
Steam reforming performance in a coupled reactor that consists of a steam reformer and a catalytic combustor is experimentally investigated in this study.
The second step is to calculate and validate reforming performance with kinetic model.
Both particle size and the interaction between NiO and CeO2 determined the reforming performance.
The reforming performance was best among the test conditions when the mixture ratio of 70 wt% H2O2/CH3OH was 3.036.
The design of foam structure parameters in volumetric solar reactor significantly affects the transport phenomena and overall reforming performance.
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Thermal and reforming performances in different configurations are compared in detail.
Best dry reforming performances are achieved with catalyst compositions having low Ni (2 wt%), ZrO2 (<1 wt%) and high CeO2 (>3 wt%) content.
The methanol-steam reforming (MSR) performance in micro-scale tubular reformers made by various materials is numerically studied.
High efficiency methanol steam reforming catalyst performance has been demonstrated which implies a feasibility in designing a high performance methanol steam reformer with reduced volume for portable device applications.
The results show that the characteristic ratios have significant effects on the transport phenomena and overall reforming reaction performance.
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