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    <subfield code="a">10.1016/j.fuproc.2015.05.034</subfield>
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    <subfield code="2">sideral</subfield>
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    <subfield code="a">eng</subfield>
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  <datafield tag="100" ind1=" " ind2=" ">
    <subfield code="a">Remón, J.</subfield>
    <subfield code="u">Universidad de Zaragoza</subfield>
    <subfield code="0">(orcid)0000-0003-3315-5933</subfield>
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  <datafield tag="245" ind1=" " ind2=" ">
    <subfield code="a">Effect of acetic acid, methanol and potassium hydroxide on the catalytic steam reforming of glycerol: Thermodynamic and experimental study</subfield>
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  <datafield tag="260" ind1=" " ind2=" ">
    <subfield code="c">2015</subfield>
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    <subfield code="a">Access copy available to the general public</subfield>
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    <subfield code="a">The present work analyses the effect on the reforming process of biodiesel crude glycerol of three impurities commonly found in this product. The influence of the presence of CH3OH (0–5 wt.%) and/or CH3COOH (0–3 wt.%) and/or KOH (0–2.8 wt.%) during the catalytic steam reforming of a 30 wt.% glycerol aqueous solution has been evaluated theoretically, studying the equilibrium composition of the gas, and experimentally in a fluidised bed reactor at 550 °C. The presence of the aforementioned impurities has a weak impact on the thermodynamic gas composition. However, they significantly influence the product distribution (in carbon basis) obtained experimentally. The carbon of the feed converted into gas, solid and liquid products varied as follows: 75–100%, 0–25% and 0–2.5%. CH3OH alone does not alter the results obtained with pure glycerol. In contrast, CH3COOH and KOH decrease the initial production of gases. This decrease is very high for KOH due to the formation of char. However, its progressive accumulation inside the reactor exerts a positive catalytic effect on the gasification of this char, augmenting the gas production over time. The composition of the gas was little affected by the presence of the impurities. The gas phase was made up of a mixture of H2 (66–70 vol.%), CO2 (24–29 vol.%), CO (3–6 vol.%) and CH4 (0.5–2.5 vol.%). The liquid phase consisted of a mixture of alcohols, ketones, cyclic compounds, aldehydes and phenols</subfield>
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    <subfield code="9">info:eu-repo/grantAgreement/ES/MINECO/ENE2010-18985</subfield>
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    <subfield code="9">info:eu-repo/semantics/openAccess</subfield>
    <subfield code="a">All rights reserved</subfield>
    <subfield code="u">http://www.europeana.eu/rights/rr-f/</subfield>
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    <subfield code="b">9 / 72 = 0.125</subfield>
    <subfield code="c">2015</subfield>
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    <subfield code="b">18 / 135 = 0.133</subfield>
    <subfield code="c">2015</subfield>
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    <subfield code="a">ENERGY &amp; FUELS</subfield>
    <subfield code="b">19 / 88 = 0.216</subfield>
    <subfield code="c">2015</subfield>
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    <subfield code="a">Chemical Engineering (miscellaneous)</subfield>
    <subfield code="c">2015</subfield>
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  <datafield tag="593" ind1=" " ind2=" ">
    <subfield code="a">Fuel Technology</subfield>
    <subfield code="c">2015</subfield>
    <subfield code="d">Q1</subfield>
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  <datafield tag="593" ind1=" " ind2=" ">
    <subfield code="a">Energy Engineering and Power Technology</subfield>
    <subfield code="c">2015</subfield>
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    <subfield code="v">info:eu-repo/semantics/acceptedVersion</subfield>
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  <datafield tag="700" ind1=" " ind2=" ">
    <subfield code="a">Mercado, V.</subfield>
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  <datafield tag="700" ind1=" " ind2=" ">
    <subfield code="a">García, L.</subfield>
    <subfield code="u">Universidad de Zaragoza</subfield>
    <subfield code="0">(orcid)0000-0001-7115-9025</subfield>
  </datafield>
  <datafield tag="700" ind1=" " ind2=" ">
    <subfield code="a">Arauzo, J.</subfield>
    <subfield code="u">Universidad de Zaragoza</subfield>
    <subfield code="0">(orcid)0000-0002-5959-3168</subfield>
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    <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">138 (2015), 325-336</subfield>
    <subfield code="p">Fuel process. technol.</subfield>
    <subfield code="t">Fuel Processing Technology</subfield>
    <subfield code="x">0378-3820</subfield>
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