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ANALYSIS OF AUTOTHERMAL REFORMER OF H_2 PRODUCTION FOR PROTON EXCHANGE MEMBRANE FUEL CELL VEHICLES

Sheng Wang

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Abstract

The coupling of oxidation of methanol (a strong exothermic process) with the steam reforming reaction(a high endothermic process) is an attractive route for H 2 production in terms of energy minimization. Analysis showed that the radial reactor is the most attractive configuration for on board H 2 generation. Using a one dimensional homogeneous model, the paper discussed the performance of this self evident process. The optimal rate of water to methanol and pressure are 2 (under normal pressure) or 3 (when P1?atm) and 0.2?MPa~0.3?MPa, respectively.

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The coupling of oxidation of methanol (a strong exothermic process) with the steam reforming reaction(a high endothermic process) is an attractive route for H 2 production in terms of energy minimization. Analysis showed that the radial reactor is the most attractive configuration for on board H 2 generation. Using a one dimensional homogeneous model, the paper discussed the performance of this self evident process. The optimal rate of water to methanol and pressure are 2 (under normal pressure) or 3 (when P1?atm) and 0.2?MPa~0.3?MPa, respectively.

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Available abstract

The coupling of oxidation of methanol (a strong exothermic process) with the steam reforming reaction(a high endothermic process) is an attractive route for H 2 production in terms of energy minimization. Analysis showed that the radial reactor is the most attractive configuration for on board H 2 generation. Using a one dimensional homogeneous model, the paper discussed the performance of this self evident process. The optimal rate of water to methanol and pressure are 2 (under normal pressure) or 3 (when P1?atm) and 0.2?MPa~0.3?MPa, respectively.

Key concepts: Chemistry, Exothermic reaction, Endothermic process, Methanol, Steam reforming, Proton exchange membrane fuel cell, Methane reformer, Coupling (piping)

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