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    Experimental Framework for Evaluation of the Thermodynamic and Kinetic Parameters of Metal-Oxides for Solar Thermochemical Fuel Production

    Source: Journal of Solar Energy Engineering:;2019:;volume( 141 ):;issue: 002::page 21007
    Author:
    Carrillo, Richard J.
    ,
    Warren, Kent J.
    ,
    Scheffe, Jonathan R.
    DOI: 10.1115/1.4042088
    Publisher: The American Society of Mechanical Engineers (ASME)
    Abstract: The two-step metal oxide redox cycle is a promising and thermodynamically attractive means of solar fuel production. In this work, we describe the development of a high-temperature tubular reactor in which the fundamental thermodynamic and kinetic behavior of thermochemical materials can be readily assessed. This reactor system is capable of operating at temperatures up to 1873 K, total pressures ranging from vacuum to ambient, and oxygen partial pressures (pO2) as low as 10−29 atm. Compared to off-the-shelf systems like thermogravimetric analyzers or indirect conductivity-based measurement systems, this system has three inherent benefits: (1) the flexibility to control the sample morphology (e.g., powder, packed bed, reticulated porous ceramic, or pellet), (2) the potential for a well-developed and characterized flow, and (3) the ability to readily customize the system on demand (e.g., easy integration with a steam generator to control and operate at very low pO2). The reactor system and experimental methods were validated by performing isothermal relaxation experiments with undoped ceria, wherein the sample environment was rapidly altered by stepwise changes in the delivered H2O vapor concentration, and comparing measured oxygen nonstoichiometries with accepted data available in the literature. Data were measured at temperatures from 1173 to 1473 K and pO2 from 4.54  × 10−18 to 1.02 × 10−9 atm. The measured equilibrium data displayed strong agreement with the literature and the expected trends were preserved. Kinetic data were extracted by first transforming reactant concentrations measured downstream of the reaction zone using a tanks-in-series mixing model to account for gas dispersion. Next, a mechanistic kinetic model distinguishing surface and bulk species concentrations was fit to the data to extract pertinent thermodynamic and kinetic parameters. The model assumed a two-step reaction mechanism mediated by the formation of an intermediate hydroxyl species on the surface. Activation energies and defect formation enthalpies and entropies for the forward and reverse reactions were found to be in good agreement with previous modeling efforts, providing further validation of the use of this system to explore thermodynamic and kinetic behavior of emerging thermochemical materials.
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      Experimental Framework for Evaluation of the Thermodynamic and Kinetic Parameters of Metal-Oxides for Solar Thermochemical Fuel Production

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    https://yetl.yabesh.ir/yetl1/handle/yetl/4256788
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    contributor authorCarrillo, Richard J.
    contributor authorWarren, Kent J.
    contributor authorScheffe, Jonathan R.
    date accessioned2019-03-17T11:10:49Z
    date available2019-03-17T11:10:49Z
    date copyright1/8/2019 12:00:00 AM
    date issued2019
    identifier issn0199-6231
    identifier othersol_141_02_021007.pdf
    identifier urihttp://yetl.yabesh.ir/yetl1/handle/yetl/4256788
    description abstractThe two-step metal oxide redox cycle is a promising and thermodynamically attractive means of solar fuel production. In this work, we describe the development of a high-temperature tubular reactor in which the fundamental thermodynamic and kinetic behavior of thermochemical materials can be readily assessed. This reactor system is capable of operating at temperatures up to 1873 K, total pressures ranging from vacuum to ambient, and oxygen partial pressures (pO2) as low as 10−29 atm. Compared to off-the-shelf systems like thermogravimetric analyzers or indirect conductivity-based measurement systems, this system has three inherent benefits: (1) the flexibility to control the sample morphology (e.g., powder, packed bed, reticulated porous ceramic, or pellet), (2) the potential for a well-developed and characterized flow, and (3) the ability to readily customize the system on demand (e.g., easy integration with a steam generator to control and operate at very low pO2). The reactor system and experimental methods were validated by performing isothermal relaxation experiments with undoped ceria, wherein the sample environment was rapidly altered by stepwise changes in the delivered H2O vapor concentration, and comparing measured oxygen nonstoichiometries with accepted data available in the literature. Data were measured at temperatures from 1173 to 1473 K and pO2 from 4.54  × 10−18 to 1.02 × 10−9 atm. The measured equilibrium data displayed strong agreement with the literature and the expected trends were preserved. Kinetic data were extracted by first transforming reactant concentrations measured downstream of the reaction zone using a tanks-in-series mixing model to account for gas dispersion. Next, a mechanistic kinetic model distinguishing surface and bulk species concentrations was fit to the data to extract pertinent thermodynamic and kinetic parameters. The model assumed a two-step reaction mechanism mediated by the formation of an intermediate hydroxyl species on the surface. Activation energies and defect formation enthalpies and entropies for the forward and reverse reactions were found to be in good agreement with previous modeling efforts, providing further validation of the use of this system to explore thermodynamic and kinetic behavior of emerging thermochemical materials.
    publisherThe American Society of Mechanical Engineers (ASME)
    titleExperimental Framework for Evaluation of the Thermodynamic and Kinetic Parameters of Metal-Oxides for Solar Thermochemical Fuel Production
    typeJournal Paper
    journal volume141
    journal issue2
    journal titleJournal of Solar Energy Engineering
    identifier doi10.1115/1.4042088
    journal fristpage21007
    journal lastpage021007-10
    treeJournal of Solar Energy Engineering:;2019:;volume( 141 ):;issue: 002
    contenttypeFulltext
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