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    <subfield code="a">10.1016/j.ijhydene.2013.07.015</subfield>
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    <subfield code="2">sideral</subfield>
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    <subfield code="a">ART-2014-85416</subfield>
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    <subfield code="a">eng</subfield>
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  <datafield tag="100" ind1=" " ind2=" ">
    <subfield code="a">Romero-Pascual, E.</subfield>
    <subfield code="u">Universidad de Zaragoza</subfield>
    <subfield code="0">(orcid)0000-0001-7814-2277</subfield>
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  <datafield tag="245" ind1=" " ind2=" ">
    <subfield code="a">Modelling of an HTPEM-based micro-combined heat and power fuel cell system with methanol</subfield>
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  <datafield tag="260" ind1=" " ind2=" ">
    <subfield code="c">2014</subfield>
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    <subfield code="a">A fuel cell-based combined heat and power system using a high temperature proton exchange membrane fuel cell has been modelled. The fuel cell is fed with the outlet hydrogen stream from a methanol steam reforming reactor. In order to provide the necessary heat to this reactor, it was considered the use of a catalytic combustor fed with methanol. The modelling aims to fit the hydrogen production to the demand of the fuel cell to provide 1 kWe, maintaining a CO concentration always lower than 30,000 ppm. A system with 65 cells (45.16 cm2 cell area) stack operating at 150 °C and hydrogen utilization factor = 0.9 (with O2/methanol ratio = 2 at combustor; H2O/methanol ratio = 2 and temperature = 300 °C at reformer) needed a total methanol flow of 23.8 mol h−1 (0.96 L h−1) to reach 1 kWe, with a system power efficiency (LHV basis) ca. 24% and a CHP efficiency over 87%. The ability to recycle the non-converted hydrogen from the fuel cell anode to the combustor and to use the heat produced at the fuel cell for obtaining hot water increased the global energy efficiency.</subfield>
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    <subfield code="a">CHEMISTRY, PHYSICAL</subfield>
    <subfield code="b">43 / 138 = 0.312</subfield>
    <subfield code="c">2014</subfield>
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  <datafield tag="591" ind1=" " ind2=" ">
    <subfield code="a">ENERGY &amp; FUELS</subfield>
    <subfield code="b">25 / 89 = 0.281</subfield>
    <subfield code="c">2014</subfield>
    <subfield code="d">Q2</subfield>
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    <subfield code="a">ELECTROCHEMISTRY</subfield>
    <subfield code="b">7 / 27 = 0.259</subfield>
    <subfield code="c">2014</subfield>
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  <datafield tag="700" ind1=" " ind2=" ">
    <subfield code="a">Soler, J.</subfield>
    <subfield code="u">Universidad de Zaragoza</subfield>
    <subfield code="0">(orcid)0000-0001-9022-2835</subfield>
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  <datafield tag="710" ind1="2" ind2=" ">
    <subfield code="1">5005</subfield>
    <subfield code="2">555</subfield>
    <subfield code="a">Universidad de Zaragoza</subfield>
    <subfield code="b">Dpto. Ing.Quím.Tecnol.Med.Amb.</subfield>
    <subfield code="c">Área Ingeniería Química</subfield>
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  <datafield tag="773" ind1=" " ind2=" ">
    <subfield code="g">39, 8 (2014), 4053-4059</subfield>
    <subfield code="p">Int. j. hydrogen energy</subfield>
    <subfield code="t">International Journal of Hydrogen Energy</subfield>
    <subfield code="x">0360-3199</subfield>
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