<?xml version="1.0" encoding="UTF-8"?>
<collection xmlns="http://www.loc.gov/MARC21/slim">
    <record>
        <controlfield tag="001">58347</controlfield>
        <controlfield tag="005">20200221144244.0</controlfield>
        <datafield tag="024" ind1="7" ind2=" ">
            <subfield code="2">doi</subfield>
            <subfield code="a">10.1016/j.cej.2015.08.127</subfield>
        </datafield>
        <datafield tag="024" ind1="8" ind2=" ">
            <subfield code="2">sideral</subfield>
            <subfield code="a">92828</subfield>
        </datafield>
        <datafield tag="037" ind1=" " ind2=" ">
            <subfield code="a">ART-2016-92828</subfield>
        </datafield>
        <datafield tag="041" ind1=" " ind2=" ">
            <subfield code="a">eng</subfield>
        </datafield>
        <datafield tag="100" ind1=" " ind2=" ">
            <subfield code="0">(orcid)0000-0003-3211-0485</subfield>
            <subfield code="a">Julián, I.</subfield>
        </datafield>
        <datafield tag="245" ind1=" " ind2=" ">
            <subfield code="a">Gas permeation effect on the Two-Section Two-Zone Fluidized Bed Membrane Reactor (TS-TZFBMR) fluid dynamics: A CFD simulation study</subfield>
        </datafield>
        <datafield tag="260" ind1=" " ind2=" ">
            <subfield code="c">2016</subfield>
        </datafield>
        <datafield tag="506" ind1="0" ind2=" ">
            <subfield code="a">Access copy available to the general public</subfield>
            <subfield code="f">Unrestricted</subfield>
        </datafield>
        <datafield tag="520" ind1="3" ind2=" ">
            <subfield code="a">Two-Fluid Model simulations were conducted using the commercial software Ansys CFX and Fluent to study the effect of the gas extraction on the fluid dynamic behavior of a membrane-assisted Two-Section Two-Zone Fluidized Bed Membrane Reactor (TS-TZFBMR). Simulated bubble properties and bed dynamics were analyzed and compared among different membrane reactor configurations, including reactor-wall (RWM) and immersed tubular (ITM) membranes, for their future use in catalytic reactions, e.g., alkane dehydrogenation or methane steam reforming. According to the solids hold-up distribution at different fluidization regimes and permeation fluxes, the ITM configuration is the most suitable to enhance the gas-particle contact and to favor the solids axial mixing for in-situ catalyst regeneration purposes. However, the RWM configuration provides a greater permeation area for selective gas removal and is preferred to enhance purification. It was found that relative permeation fluxes above 20% of the total feed gas have a significant impact on the fluid dynamic regime within the TS-TZFBMR, concerning the appearance of local defluidized regions, gas channeling and solids axial mixing.</subfield>
        </datafield>
        <datafield tag="536" ind1=" " ind2=" ">
            <subfield code="9">info:eu-repo/grantAgreement/ES/MINECO/CTQ2010-15568</subfield>
            <subfield code="9">info:eu-repo/grantAgreement/ES/MINECO/ENE2013-44350-R</subfield>
        </datafield>
        <datafield tag="540" ind1=" " ind2=" ">
            <subfield code="9">info:eu-repo/semantics/openAccess</subfield>
            <subfield code="a">by-nc-nd</subfield>
            <subfield code="u">http://creativecommons.org/licenses/by-nc-nd/3.0/es/</subfield>
        </datafield>
        <datafield tag="590" ind1=" " ind2=" ">
            <subfield code="a">6.216</subfield>
            <subfield code="b">2016</subfield>
        </datafield>
        <datafield tag="591" ind1=" " ind2=" ">
            <subfield code="a">ENGINEERING, ENVIRONMENTAL</subfield>
            <subfield code="b">3 / 49 = 0.061</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
            <subfield code="e">T1</subfield>
        </datafield>
        <datafield tag="591" ind1=" " ind2=" ">
            <subfield code="a">ENGINEERING, CHEMICAL</subfield>
            <subfield code="b">6 / 135 = 0.044</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
            <subfield code="e">T1</subfield>
        </datafield>
        <datafield tag="592" ind1=" " ind2=" ">
            <subfield code="a">1.758</subfield>
            <subfield code="b">2016</subfield>
        </datafield>
        <datafield tag="593" ind1=" " ind2=" ">
            <subfield code="a">Chemical Engineering (miscellaneous)</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
        </datafield>
        <datafield tag="593" ind1=" " ind2=" ">
            <subfield code="a">Industrial and Manufacturing Engineering</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
        </datafield>
        <datafield tag="593" ind1=" " ind2=" ">
            <subfield code="a">Environmental Chemistry</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
        </datafield>
        <datafield tag="593" ind1=" " ind2=" ">
            <subfield code="a">Chemistry (miscellaneous)</subfield>
            <subfield code="c">2016</subfield>
            <subfield code="d">Q1</subfield>
        </datafield>
        <datafield tag="655" ind1=" " ind2="4">
            <subfield code="a">info:eu-repo/semantics/article</subfield>
            <subfield code="v">info:eu-repo/semantics/acceptedVersion</subfield>
        </datafield>
        <datafield tag="700" ind1=" " ind2=" ">
            <subfield code="0">(orcid)0000-0003-1940-9597</subfield>
            <subfield code="a">Herguido, J.</subfield>
            <subfield code="u">Universidad de Zaragoza</subfield>
        </datafield>
        <datafield tag="700" ind1=" " ind2=" ">
            <subfield code="0">(orcid)0000-0002-2494-102X</subfield>
            <subfield code="a">Menéndez, M.</subfield>
            <subfield code="u">Universidad de Zaragoza</subfield>
        </datafield>
        <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>
        </datafield>
        <datafield tag="773" ind1=" " ind2=" ">
            <subfield code="g">301 (2016), 201-211</subfield>
            <subfield code="p">Chem. eng. j.</subfield>
            <subfield code="t">Chemical Engineering Journal</subfield>
            <subfield code="x">1385-8947</subfield>
        </datafield>
        <datafield tag="856" ind1="4" ind2=" ">
            <subfield code="s">761141</subfield>
            <subfield code="u">http://zaguan.unizar.es/record/58347/files/texto_completo.pdf</subfield>
            <subfield code="y">Postprint</subfield>
        </datafield>
        <datafield tag="856" ind1="4" ind2=" ">
            <subfield code="s">100360</subfield>
            <subfield code="u">http://zaguan.unizar.es/record/58347/files/texto_completo.jpg?subformat=icon</subfield>
            <subfield code="x">icon</subfield>
            <subfield code="y">Postprint</subfield>
        </datafield>
        <datafield tag="909" ind1="C" ind2="O">
            <subfield code="o">oai:zaguan.unizar.es:58347</subfield>
            <subfield code="p">articulos</subfield>
            <subfield code="p">driver</subfield>
        </datafield>
        <datafield tag="951" ind1=" " ind2=" ">
            <subfield code="a">2020-02-21-13:23:16</subfield>
        </datafield>
        <datafield tag="980" ind1=" " ind2=" ">
            <subfield code="a">ARTICLE</subfield>
        </datafield>
    </record>

    
</collection>