<?xml version="1.0" encoding="ISO-8859-1"?><article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance">
<front>
<journal-meta>
<journal-id>1909-3667</journal-id>
<journal-title><![CDATA[Tecciencia]]></journal-title>
<abbrev-journal-title><![CDATA[Tecciencia]]></abbrev-journal-title>
<issn>1909-3667</issn>
<publisher>
<publisher-name><![CDATA[Universidad ECCI]]></publisher-name>
</publisher>
</journal-meta>
<article-meta>
<article-id>S1909-36672018000200055</article-id>
<article-id pub-id-type="doi">10.18180/tecciencia.2018.25.7</article-id>
<title-group>
<article-title xml:lang="en"><![CDATA[Hydrogen Production and Purification by Bioethanol Steam Reforming and Preferential Oxidation of CO]]></article-title>
<article-title xml:lang="es"><![CDATA[Producción y Purificación de Hidrógeno por Reformado de Vapor de Bioetanol y Oxidación Selectiva de CO]]></article-title>
</title-group>
<contrib-group>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Arévalo]]></surname>
<given-names><![CDATA[Juan David]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Martinez-Hernández]]></surname>
<given-names><![CDATA[Ángel]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Vargas]]></surname>
<given-names><![CDATA[Julio César]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
<contrib contrib-type="author">
<name>
<surname><![CDATA[Córdoba]]></surname>
<given-names><![CDATA[Luis Fernando]]></given-names>
</name>
<xref ref-type="aff" rid="Aff"/>
</contrib>
</contrib-group>
<aff id="Af1">
<institution><![CDATA[,Universidad Nacional de Colombia Departamento de Ingeniería Química y Ambiental ]]></institution>
<addr-line><![CDATA[Bogotá ]]></addr-line>
<country>Colombia</country>
</aff>
<aff id="Af2">
<institution><![CDATA[,Universidad Autónoma de Nuevo León Facultad de Ciencias Químicas ]]></institution>
<addr-line><![CDATA[ ]]></addr-line>
<country>Mexico</country>
</aff>
<pub-date pub-type="pub">
<day>00</day>
<month>12</month>
<year>2018</year>
</pub-date>
<pub-date pub-type="epub">
<day>00</day>
<month>12</month>
<year>2018</year>
</pub-date>
<volume>13</volume>
<numero>25</numero>
<fpage>55</fpage>
<lpage>64</lpage>
<copyright-statement/>
<copyright-year/>
<self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_arttext&amp;pid=S1909-36672018000200055&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_abstract&amp;pid=S1909-36672018000200055&amp;lng=en&amp;nrm=iso"></self-uri><self-uri xlink:href="http://www.scielo.org.co/scielo.php?script=sci_pdf&amp;pid=S1909-36672018000200055&amp;lng=en&amp;nrm=iso"></self-uri><abstract abstract-type="short" xml:lang="en"><p><![CDATA[Abstract Hydrogen production and purification was studied in a combined system including double catalytic bed reaction system. Steam Reforming of Ethanol (SRE) was performed in Ni/CeO2-ZrO2 catalyst and, subsequently, the reforming products gases passed through a second fixed bed containing Au/CeO2-ZrO2 catalyst in order to carry out the preferential CO oxidation (PROX-CO). Initially, the effect of temperature and the initial water concentration in the fed ethanol were evaluated to determine the conditions that maximize the H2/CO ratio while maintaining 100% conversion of ethanol. These requirements were accomplished when 25 mole% H2O and 4 mole% C2H5OH (steam/ethanol molar ratio = 7) were used. The catalyst stability was assessed under these reaction conditions at 600°C, during more than 160 h on stream, obtaining ethanol conversions above 99% during the entire test and H2 productivity close to ideal. In the second part of the work, in order to obtain H2 grade PEM, the effect of O2 concentration in the feed stream on the selective CO oxidation using Au-CZ catalysts was investigated in the temperature range of 50-250°C. Catalytic stability test was also performed. Characterization techniques: Temperature Programmed Reduction (TPR), X-Ray Diffraction (XRD), SEM-EDX, which confirmed the presence of a strong interaction between the mixed oxide support and the metal. In this study, we show a reaction system with double catalytic fixed bed in which hydrogen is obtained with the specifications required by PEM fuel cell. The tested materials exhibit high activity and selectivity towards hydrogen production and CO selective oxidation in the range of temperature studied.]]></p></abstract>
<abstract abstract-type="short" xml:lang="es"><p><![CDATA[Resumen La producción y purificación de hidrógeno fue estudiada en un sistema combinado incluyendo un doble lecho catalítico. El reformado de etanol con vapor de agua (SER) fue realizado con un catalizador de Ni/CeO2-ZrO2 y, posteriormente, los productos gaseosos del reformado pasaron por un segundo lecho catalítico que contiene un catalizador de Au/CeO2-ZrO2, para llevar a cabo la oxidación preferencial de CO (PROX-CO). Inicialmente, el efecto de la temperatura y la concentración inicial de agua en el alimento de etanol fueron evaluados para determinar las condiciones que maximizan la relación H2/CO mientras se mantiene una conversión del 100% de etanol. Estos requerimientos se lograron con 25 mol% H2O y 4 mol% C2H5OH (vapor de agua/etanol relación molar = 7). La estabilidad catalítica fue evaluada a esas condiciones de reacción a 600°C, durante más de 160 h, obteniendo conversiones por encima de 99% en todo el ensayo y una productividad de H2 cercana a la ideal. En la segunda parte del trabajo, para obtener H2 grado PEM, se estudió el efecto de la concentración de O2 en la corriente de alimento a la oxidación selectiva de CO usando el catalizador Au-CZ en el rango de 50-250°C. La prueba de estabilidad también fue realizada. Técnicas de caracterización: Reducción a Temperatura Programada (TPR), Difracción de Rayos X (XRD), SEM-EDX, las cuales confirmaron la presencia de una fuerte interacción entre el soporte de óxido mixto y el metal. En este estudio, se presenta un sistema de reacción con doble lecho catalítico en el cual el hidrógeno es obtenido con las especificaciones requeridas por las celdas de combustible PEM. Los materiales ensayados exhibieron una alta actividad y selectividad hacia la producción de hidrógeno y oxidación selectiva de CO en el rango de temperatura evaluado.]]></p></abstract>
<kwd-group>
<kwd lng="en"><![CDATA[Ni/CeO2-ZrO2 catalyst]]></kwd>
<kwd lng="en"><![CDATA[Au/CeO2-ZrO2 catalyst]]></kwd>
<kwd lng="en"><![CDATA[Steam reforming]]></kwd>
<kwd lng="en"><![CDATA[Ethanol]]></kwd>
<kwd lng="en"><![CDATA[Hydrogen production]]></kwd>
<kwd lng="en"><![CDATA[PROX-CO]]></kwd>
<kwd lng="es"><![CDATA[Catalizador Ni/CeO2-ZrO2]]></kwd>
<kwd lng="es"><![CDATA[Catalizador Au/CeO2-ZrO2]]></kwd>
<kwd lng="es"><![CDATA[Reformado de vapor]]></kwd>
<kwd lng="es"><![CDATA[Etanol]]></kwd>
<kwd lng="es"><![CDATA[Producción de Hidrógeno]]></kwd>
<kwd lng="es"><![CDATA[PROX-CO]]></kwd>
</kwd-group>
</article-meta>
</front><back>
<ref-list>
<ref id="B1">
<label>1</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lior]]></surname>
<given-names><![CDATA[N.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Energy resources and use: The present situation and possible paths to the future]]></article-title>
<source><![CDATA[Energy]]></source>
<year>2008</year>
<volume>33</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>842-57</page-range></nlm-citation>
</ref>
<ref id="B2">
<label>2</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ni]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Leung]]></surname>
<given-names><![CDATA[D. Y. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Leung]]></surname>
<given-names><![CDATA[M. K. H.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[A review on reforming bio-ethanol for hydrogen production]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2007</year>
<volume>32</volume>
<page-range>3238-47</page-range></nlm-citation>
</ref>
<ref id="B3">
<label>3</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ni]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Leung]]></surname>
<given-names><![CDATA[D. Y. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Leung]]></surname>
<given-names><![CDATA[M. K. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Sumathy]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[An overview of hydrogen production from biomass]]></article-title>
<source><![CDATA[Fuel Process. Technol]]></source>
<year>2006</year>
<volume>87</volume>
<page-range>461-72</page-range></nlm-citation>
</ref>
<ref id="B4">
<label>4</label><nlm-citation citation-type="">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Show]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
<name>
<surname><![CDATA[Lee]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Zhang]]></surname>
<given-names><![CDATA[Z.]]></given-names>
</name>
</person-group>
<source><![CDATA[Biofuels]]></source>
<year>2011</year>
<page-range>467-79</page-range></nlm-citation>
</ref>
<ref id="B5">
<label>5</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Haryanto]]></surname>
<given-names><![CDATA[S]]></given-names>
</name>
<name>
<surname><![CDATA[Murali]]></surname>
<given-names><![CDATA[Fernando, N]]></given-names>
</name>
<name>
<surname><![CDATA[Adhikari]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Current status of hydrogen production techniques by steam reforming of ethanol: A review]]></article-title>
<source><![CDATA[Energy and Fuels]]></source>
<year>2005</year>
<volume>19</volume>
<numero>10</numero>
<issue>10</issue>
<page-range>2098-106</page-range></nlm-citation>
</ref>
<ref id="B6">
<label>6</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Cobo]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Pieruccini]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Abello]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Ariza]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Córdoba]]></surname>
<given-names><![CDATA[L. F.]]></given-names>
</name>
<name>
<surname><![CDATA[Conesa]]></surname>
<given-names><![CDATA[J. a.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Steam reforming of ethanol over bimetallic RhPt/La2O3: Long-term stability under favorable reaction conditions]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2013</year>
<volume>38</volume>
<page-range>5580-93</page-range></nlm-citation>
</ref>
<ref id="B7">
<label>7</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Biswas]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Kunzru]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Oxidative steam reforming of ethanol over Ni/CeO2-ZrO2 catalyst]]></article-title>
<source><![CDATA[Chem. Eng. J]]></source>
<year>2008</year>
<volume>136</volume>
<page-range>41-9</page-range></nlm-citation>
</ref>
<ref id="B8">
<label>8</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Manzolini]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Tosti]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Hydrogen production from ethanol steam reforming: energy efficiency analysis of traditional and membrane processes]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2008</year>
<volume>33</volume>
<numero>20</numero>
<issue>20</issue>
<page-range>5571-82</page-range></nlm-citation>
</ref>
<ref id="B9">
<label>9</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Arango-Díaz]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Moretti]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Talon]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Storaro]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Lenarda]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Núñez]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Marrero-Jerez]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Jiménez-Jiménez]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Jiménez-López]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Rodríguez-Castellón]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Preferential CO oxidation (CO-PROX) catalyzed by CuO supported on nanocrystalline CeO2 prepared by a freeze-drying method]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2014</year>
<volume>477</volume>
<page-range>54-63</page-range></nlm-citation>
</ref>
<ref id="B10">
<label>10</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Reyes-Carmona]]></surname>
<given-names><![CDATA[Á.]]></given-names>
</name>
<name>
<surname><![CDATA[Arango-Díaz]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Moretti]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Talon]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Storaro]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Lenarda]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Jiménez-López]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Rodríguez-Castellón]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[CuO/CeO2 supported on Zr doped SBA-15 as catalysts for preferential CO oxidation (CO-PROX)]]></article-title>
<source><![CDATA[J. Power Sources]]></source>
<year>2011</year>
<volume>196</volume>
<numero>9</numero>
<issue>9</issue>
<page-range>4382-7</page-range></nlm-citation>
</ref>
<ref id="B11">
<label>11</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lima]]></surname>
<given-names><![CDATA[S. M. de]]></given-names>
</name>
<name>
<surname><![CDATA[Colman]]></surname>
<given-names><![CDATA[R. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Jacobs]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Davis]]></surname>
<given-names><![CDATA[B. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Souza]]></surname>
<given-names><![CDATA[K. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Lima]]></surname>
<given-names><![CDATA[A. F. F. de]]></given-names>
</name>
<name>
<surname><![CDATA[Appel]]></surname>
<given-names><![CDATA[L. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Mattos]]></surname>
<given-names><![CDATA[L. V.]]></given-names>
</name>
<name>
<surname><![CDATA[Noronha]]></surname>
<given-names><![CDATA[F. B.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Hydrogen production from ethanol for PEM fuel cells. An integrated fuel processor comprising ethanol steam reforming and preferential oxidation of CO]]></article-title>
<source><![CDATA[Catal. Today]]></source>
<year>2009</year>
<volume>146</volume>
<page-range>110-23</page-range></nlm-citation>
</ref>
<ref id="B12">
<label>12</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sahoo]]></surname>
<given-names><![CDATA[D. R.]]></given-names>
</name>
<name>
<surname><![CDATA[Vajpai]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Patel]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Pant]]></surname>
<given-names><![CDATA[K. K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Kinetic modeling of steam reforming of ethanol for the production of hydrogen over Co/Al2O3 catalyst]]></article-title>
<source><![CDATA[Chem. Eng. J]]></source>
<year>2007</year>
<volume>125</volume>
<page-range>139-47</page-range></nlm-citation>
</ref>
<ref id="B13">
<label>13</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Biswas]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Kunzru]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Steam reforming of ethanol for production of hydrogen over Ni/CeO2-ZrO2 catalyst: Effect of support and metal loading]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2007</year>
<volume>32</volume>
<page-range>969-80</page-range></nlm-citation>
</ref>
<ref id="B14">
<label>14</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Fonseca]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Royer]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Bion]]></surname>
<given-names><![CDATA[N.]]></given-names>
</name>
<name>
<surname><![CDATA[Pirault-Roy]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[C. Rangel]]></surname>
<given-names><![CDATA[M. do]]></given-names>
</name>
<name>
<surname><![CDATA[Duprez]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Epron]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Preferential CO oxidation over nanosized gold catalysts supported on ceria and amorphous ceria - alumina]]></article-title>
<source><![CDATA[Applied Catal. B, Environ]]></source>
<year>2012</year>
<volume>128</volume>
<page-range>10-20</page-range></nlm-citation>
</ref>
<ref id="B15">
<label>15</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Mondal]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
<name>
<surname><![CDATA[Pant]]></surname>
<given-names><![CDATA[K. K.]]></given-names>
</name>
<name>
<surname><![CDATA[Dalai]]></surname>
<given-names><![CDATA[A. K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Catalytic oxidative steam reforming of bio-ethanol for hydrogen production over Rh promoted Ni/CeO2-ZrO2 catalyst]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2015</year>
<volume>40</volume>
<numero>6</numero>
<issue>6</issue>
<page-range>2529-44</page-range></nlm-citation>
</ref>
<ref id="B16">
<label>16</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Laguna]]></surname>
<given-names><![CDATA[O. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Centeno]]></surname>
<given-names><![CDATA[M. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Arzamendi]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Gandía]]></surname>
<given-names><![CDATA[L. M.]]></given-names>
</name>
<name>
<surname><![CDATA[Romero-Sarria]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Odriozola]]></surname>
<given-names><![CDATA[J. A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Iron-modified ceria and Au/ceria catalysts for total and preferential oxidation of CO (TOX and PROX)]]></article-title>
<source><![CDATA[Catal. Today]]></source>
<year>2010</year>
<volume>157</volume>
<page-range>1-pp. 155-159</page-range></nlm-citation>
</ref>
<ref id="B17">
<label>17</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Diagne]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Idriss]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Pearson]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
<name>
<surname><![CDATA[Gómez-García]]></surname>
<given-names><![CDATA[M. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Kiennemann]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Efficient hydrogen production by ethanol reforming over Rh catalysts. Effect of addition of Zr on CeO2 for the oxidation of CO to CO2]]></article-title>
<source><![CDATA[Comptes Rendus Chim]]></source>
<year>2004</year>
<volume>7</volume>
<page-range>617-22</page-range></nlm-citation>
</ref>
<ref id="B18">
<label>18</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Moretti]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
<name>
<surname><![CDATA[Storaro]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Talon]]></surname>
<given-names><![CDATA[a.]]></given-names>
</name>
<name>
<surname><![CDATA[Chitsazan]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Garbarino]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Busca]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Finocchio]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Ceria-zirconia based catalysts for ethanol steam reforming]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2015</year>
<volume>153</volume>
<page-range>166-75</page-range></nlm-citation>
</ref>
<ref id="B19">
<label>19</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Muroyama]]></surname>
<given-names><![CDATA[H.]]></given-names>
</name>
<name>
<surname><![CDATA[Nakase]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Matsui]]></surname>
<given-names><![CDATA[T.]]></given-names>
</name>
<name>
<surname><![CDATA[Eguchi]]></surname>
<given-names><![CDATA[K.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Ethanol steam reforming over Ni-based spinel oxide]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2010</year>
<volume>35</volume>
<numero>4</numero>
<issue>4</issue>
<page-range>1575-81</page-range></nlm-citation>
</ref>
<ref id="B20">
<label>20</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sun]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Qiu]]></surname>
<given-names><![CDATA[X. P.]]></given-names>
</name>
<name>
<surname><![CDATA[Wu]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Zhu]]></surname>
<given-names><![CDATA[W. T.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[H2 from steam reforming of ethanol at low temperature over Ni/Y2O3 and Ni/La2O3 catalysts for fuel-cell application]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2005</year>
<volume>30</volume>
<page-range>437-45</page-range></nlm-citation>
</ref>
<ref id="B21">
<label>21</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Dong]]></surname>
<given-names><![CDATA[W. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Roh]]></surname>
<given-names><![CDATA[H. S.]]></given-names>
</name>
<name>
<surname><![CDATA[Jun]]></surname>
<given-names><![CDATA[K. W.]]></given-names>
</name>
<name>
<surname><![CDATA[Park]]></surname>
<given-names><![CDATA[S. E.]]></given-names>
</name>
<name>
<surname><![CDATA[Oh]]></surname>
<given-names><![CDATA[Y. S.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Methane reforming over Ni/Ce-ZrO2 catalysts: Effect of nickel content]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2002</year>
<volume>226</volume>
<page-range>63-72</page-range></nlm-citation>
</ref>
<ref id="B22">
<label>22</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Pereira]]></surname>
<given-names><![CDATA[E. B.]]></given-names>
</name>
<name>
<surname><![CDATA[Homs]]></surname>
<given-names><![CDATA[N.]]></given-names>
</name>
<name>
<surname><![CDATA[Martí]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Fierro]]></surname>
<given-names><![CDATA[J. L. G.]]></given-names>
</name>
<name>
<surname><![CDATA[Ramírez de la Piscina]]></surname>
<given-names><![CDATA[P]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Oxidative steam-reforming of ethanol over Co/SiO2, Co-Rh/SiO2 and Co-Ru/SiO2 catalysts: Catalytic behavior and deactivation/regeneration processes]]></article-title>
<source><![CDATA[J. Catal]]></source>
<year>2008</year>
<volume>257</volume>
<page-range>206-14</page-range></nlm-citation>
</ref>
<ref id="B23">
<label>23</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Araque]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Vargas]]></surname>
<given-names><![CDATA[J. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Zimmermann]]></surname>
<given-names><![CDATA[Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Roger]]></surname>
<given-names><![CDATA[A.-C.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Study of a CeZrCoRh mixed oxide for hydrogen production by ethanol steam reforming]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2011</year>
<volume>36</volume>
<page-range>1491-502</page-range></nlm-citation>
</ref>
<ref id="B24">
<label>24</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Dan]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Mihet]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Tasnadi-Asztalos]]></surname>
<given-names><![CDATA[Z.]]></given-names>
</name>
<name>
<surname><![CDATA[Imre-Lucaci]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Katona]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Lazar]]></surname>
<given-names><![CDATA[M. D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Hydrogen production by ethanol steam reforming on nickel catalysts: Effect of support modification by CeO2 and La2O3]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2015</year>
<volume>147</volume>
<page-range>260-8</page-range></nlm-citation>
</ref>
<ref id="B25">
<label>25</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Trane-Restrup]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
<name>
<surname><![CDATA[Dahl]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Jensen]]></surname>
<given-names><![CDATA[a. D.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Steam reforming of ethanol: Effects of support and additives on Ni-based catalysts]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2013</year>
<volume>38</volume>
<numero>35</numero>
<issue>35</issue>
<page-range>15105-18</page-range></nlm-citation>
</ref>
<ref id="B26">
<label>26</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Laguna]]></surname>
<given-names><![CDATA[O. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Hernández]]></surname>
<given-names><![CDATA[W. Y.]]></given-names>
</name>
<name>
<surname><![CDATA[Arzamendi]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
<name>
<surname><![CDATA[Gandía]]></surname>
<given-names><![CDATA[L. M.]]></given-names>
</name>
<name>
<surname><![CDATA[Centeno]]></surname>
<given-names><![CDATA[M. a.]]></given-names>
</name>
<name>
<surname><![CDATA[Odriozola]]></surname>
<given-names><![CDATA[J. a.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gold supported on CuOx/CeO2 catalyst for the purification of hydrogen by the CO preferential oxidation reaction (PROX)]]></article-title>
<source><![CDATA[Fuel]]></source>
<year>2014</year>
<volume>118</volume>
<page-range>176-85</page-range></nlm-citation>
</ref>
<ref id="B27">
<label>27</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Haruta]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Daté]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Advances in the catalysis of Au nanoparticles]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2001</year>
<volume>222</volume>
<page-range>427-37</page-range></nlm-citation>
</ref>
<ref id="B28">
<label>28</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Centeno]]></surname>
<given-names><![CDATA[M. a.]]></given-names>
</name>
<name>
<surname><![CDATA[Paulis]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Montes]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Odriozola]]></surname>
<given-names><![CDATA[J. a.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Catalytic combustion of volatile organic compounds on Au/CeO2/Al2O3 and Au/Al2O3 catalysts]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2002</year>
<volume>234</volume>
<page-range>65-78</page-range></nlm-citation>
</ref>
<ref id="B29">
<label>29</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Guczi]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Horváth]]></surname>
<given-names><![CDATA[D.]]></given-names>
</name>
<name>
<surname><![CDATA[Pászti]]></surname>
<given-names><![CDATA[Z.]]></given-names>
</name>
<name>
<surname><![CDATA[Petõ]]></surname>
<given-names><![CDATA[G.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effect of treatments on gold nanoparticles: Relation between morphology, electron structure and catalytic activity in CO oxidation]]></article-title>
<source><![CDATA[Catal. Today]]></source>
<year>2002</year>
<volume>72</volume>
<page-range>101-5</page-range></nlm-citation>
</ref>
<ref id="B30">
<label>30</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Grunwaldt]]></surname>
<given-names><![CDATA[J.-D.]]></given-names>
</name>
<name>
<surname><![CDATA[Kiener]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Wögerbauer]]></surname>
<given-names><![CDATA[C.]]></given-names>
</name>
<name>
<surname><![CDATA[Baiker]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Preparation of Supported Gold Catalysts for Low-Temperature CO Oxidation via 'Size-Controlled' Gold Colloids]]></article-title>
<source><![CDATA[J. Catal]]></source>
<year>1999</year>
<volume>181</volume>
<page-range>223-32</page-range></nlm-citation>
</ref>
<ref id="B31">
<label>31</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Luengnaruemitchai]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Chawla]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Wanchanthuek]]></surname>
<given-names><![CDATA[R.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[The catalytic performance of Au/La-CeOx catalyst for PROX reaction in H2 rich stream]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2014</year>
<volume>39</volume>
<numero>30</numero>
<issue>30</issue>
<page-range>16953-63</page-range></nlm-citation>
</ref>
<ref id="B32">
<label>32</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ocampo]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Louis]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Kiwi-Minsker]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
<name>
<surname><![CDATA[Roger]]></surname>
<given-names><![CDATA[A. C.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effect of Ce/Zr composition and noble metal promotion on nickel based CexZr1-xO2 catalysts for carbon dioxide methanation]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2011</year>
<volume>392</volume>
<numero>1-2</numero>
<issue>1-2</issue>
<page-range>36-44</page-range></nlm-citation>
</ref>
<ref id="B33">
<label>33</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ocampo]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Louis]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Roger]]></surname>
<given-names><![CDATA[A.-C.]]></given-names>
</name>
<name>
<surname><![CDATA[Roger]]></surname>
<given-names><![CDATA[A.-C.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Methanation of carbon dioxide over nickel-based Ce0.72Zr0.28O2 mixed oxide catalysts prepared by sol-gel method]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2009</year>
<volume>369</volume>
<page-range>90-6</page-range></nlm-citation>
</ref>
<ref id="B34">
<label>34</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Vargas]]></surname>
<given-names><![CDATA[J. C.]]></given-names>
</name>
<name>
<surname><![CDATA[Libs]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Roger]]></surname>
<given-names><![CDATA[A.-C.]]></given-names>
</name>
<name>
<surname><![CDATA[Kiennemann]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Study of Ce-Zr-Co fluorite-type oxide as catalysts for hydrogen production by steam reforming of bioethanol]]></article-title>
<source><![CDATA[Catal. Today]]></source>
<year>2005</year>
<volume>107-108</volume>
<page-range>417-25</page-range></nlm-citation>
</ref>
<ref id="B35">
<label>35</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Lin]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Wan]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Effects of preparation conditions on gold / Y-type zeolite for CO oxidation]]></article-title>
<source><![CDATA[Appl. Catal. B Environ]]></source>
<year>2003</year>
<volume>41</volume>
<page-range>83-95</page-range></nlm-citation>
</ref>
<ref id="B36">
<label>36</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Jardim]]></surname>
<given-names><![CDATA[E. D. O.]]></given-names>
</name>
<name>
<surname><![CDATA[Rico-Francés]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Coloma]]></surname>
<given-names><![CDATA[F.]]></given-names>
</name>
<name>
<surname><![CDATA[Ramos-Fernández]]></surname>
<given-names><![CDATA[E. V.]]></given-names>
</name>
<name>
<surname><![CDATA[Silvestre-Albero]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
<name>
<surname><![CDATA[Sepúlveda-Escribano]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Superior performance of gold supported on doped CeO2 catalysts for the preferential CO oxidation (PROX)]]></article-title>
<source><![CDATA[Appl. Catal. A Gen]]></source>
<year>2014</year>
<volume>487</volume>
<page-range>119-29</page-range></nlm-citation>
</ref>
<ref id="B37">
<label>37</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Laguna]]></surname>
<given-names><![CDATA[O. H.]]></given-names>
</name>
<name>
<surname><![CDATA[Romero Sarria]]></surname>
<given-names><![CDATA[F]]></given-names>
</name>
<name>
<surname><![CDATA[Centeno]]></surname>
<given-names><![CDATA[M. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Odriozola]]></surname>
<given-names><![CDATA[J. A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Gold supported on metal-doped ceria catalysts (M = Zr, Zn and Fe) for the preferential oxidation of CO (PROX)]]></article-title>
<source><![CDATA[J. Catal]]></source>
<year>2010</year>
<volume>276</volume>
<numero>2</numero>
<issue>2</issue>
<page-range>360-70</page-range></nlm-citation>
</ref>
<ref id="B38">
<label>38</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Sun]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Yan]]></surname>
<given-names><![CDATA[W.]]></given-names>
</name>
<name>
<surname><![CDATA[Sun]]></surname>
<given-names><![CDATA[P.]]></given-names>
</name>
<name>
<surname><![CDATA[Chen]]></surname>
<given-names><![CDATA[J.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Thermodynamic analysis of ethanol reforming for hydrogen production]]></article-title>
<source><![CDATA[Energy]]></source>
<year>2012</year>
<volume>44</volume>
<numero>1</numero>
<issue>1</issue>
<page-range>911-24</page-range></nlm-citation>
</ref>
<ref id="B39">
<label>39</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Verónica]]></surname>
<given-names><![CDATA[M.]]></given-names>
</name>
<name>
<surname><![CDATA[Graciela]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Norma]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Miguel]]></surname>
<given-names><![CDATA[L.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Ethanol steam reforming using Ni(II)-Al(III) layered double hydroxide as catalyst precursor. Kinetic study]]></article-title>
<source><![CDATA[Chem. Eng. J]]></source>
<year>2008</year>
<volume>138</volume>
<page-range>602-7</page-range></nlm-citation>
</ref>
<ref id="B40">
<label>40</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Luengnaruemitchai]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
<name>
<surname><![CDATA[Osuwan]]></surname>
<given-names><![CDATA[S.]]></given-names>
</name>
<name>
<surname><![CDATA[Gulari]]></surname>
<given-names><![CDATA[E.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Selective catalytic oxidation of CO in the presence of H2 over gold catalyst]]></article-title>
<source><![CDATA[Int. J. Hydrogen Energy]]></source>
<year>2004</year>
<volume>29</volume>
<page-range>429-35</page-range></nlm-citation>
</ref>
<ref id="B41">
<label>41</label><nlm-citation citation-type="journal">
<person-group person-group-type="author">
<name>
<surname><![CDATA[Ramírez-Garza]]></surname>
<given-names><![CDATA[R. E.]]></given-names>
</name>
<name>
<surname><![CDATA[Pawelec]]></surname>
<given-names><![CDATA[B.]]></given-names>
</name>
<name>
<surname><![CDATA[Zepeda]]></surname>
<given-names><![CDATA[T. A.]]></given-names>
</name>
<name>
<surname><![CDATA[Martínez-Hernández]]></surname>
<given-names><![CDATA[A.]]></given-names>
</name>
</person-group>
<article-title xml:lang=""><![CDATA[Total CO oxidation over Fe-containing Au / HMS catalysts: Effects of gold loading and catalyst pretreatment]]></article-title>
<source><![CDATA[Catal. Today]]></source>
<year>2011</year>
<volume>172</volume>
<page-range>95-102</page-range></nlm-citation>
</ref>
</ref-list>
</back>
</article>
