Dergi makalesi Açık Erişim

Experimental and theoretical analysis of a natural gas fuel processor

Sayar, Asli; Eskin, Nurdil


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        "affiliation": "TUBITAK Marmara Res Ctr, Energy Inst, Kocaeli, Turkey", 
        "name": "Sayar, Asli"
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      {
        "affiliation": "Istanbul Tech Univ, Mech Engn Dept, Istanbul, Turkey", 
        "name": "Eskin, Nurdil"
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    "description": "In this study, a natural gas fuel processor was experimentally and theoretically investigated. The constructed 2.0 kWth fuel processor is suitable for a residential-scale high temperature proton exchange membrane fuel cell. The system consists of an autothermal reformer; gas clean-up units, namely high and low-temperature water-gas shift reactors; and utilities including feeding unit, burner, evaporator and heat exchangers. Commercial monolith catalysts were used in the reactors. The simulation was carried out by using ASPEN HYSYS program. A validated kinetic model and adiabatic equilibrium model were both presented and compared with experimental data. The nominal operating conditions which were determined by the kinetic model were the steam-to-carbon ratio of 3.0, the oxygen-to-carbon ratio of 0.5 and the inlet temperatures of 450 degrees C for autothermal reformer, 400 degrees C for high-temperature water-gas shift reactor and 310 degrees C for low-temperature water-gas shift reactor. Experimental results at the nominal condition showed that the performance criteria of the hydrogen yield, the fuel conversion and the efficiency were 2.53, 93.5% and 82.3% (higher heating value-HHV), respectively. The validated kinetic model was further used for the determination of 2-10kW thermal fuel processor efficiency which was increasing linearly up-to 86.3% (HHV). (C) 2020 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.", 
    "doi": "10.1016/j.ijhydene.2020.10.036", 
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      "issue": "2", 
      "pages": "1569-1582", 
      "title": "INTERNATIONAL JOURNAL OF HYDROGEN ENERGY", 
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