<?xml version="1.0" encoding="UTF-8"?>
<!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.3 20210610//EN" "JATS-journalpublishing1-3.dtd">
<article article-type="research-article" dtd-version="1.3" 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" xml:lang="en"><front><journal-meta><journal-id journal-id-type="publisher-id">najo</journal-id><journal-title-group><journal-title xml:lang="en">Nanosystems: Physics, Chemistry, Mathematics</journal-title><trans-title-group xml:lang="ru"><trans-title>Наносистемы: физика, химия, математика</trans-title></trans-title-group></journal-title-group><issn pub-type="ppub">2220-8054</issn><issn pub-type="epub">2305-7971</issn><publisher><publisher-name>Университет ИТМО</publisher-name></publisher></journal-meta><article-meta><article-id pub-id-type="doi">10.17586/2220-8054-2026-17-3-375-386</article-id><article-id custom-type="elpub" pub-id-type="custom">najo-1845</article-id><article-categories><subj-group subj-group-type="heading"><subject>Research Article</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="en"><subject>CHEMISTRY AND MATERIALS SCIENCE</subject></subj-group><subj-group subj-group-type="section-heading" xml:lang="ru"><subject>ХИМИЯ И НАУКА О МАТЕРИАЛАХ</subject></subj-group></article-categories><title-group><article-title>Ni/CeO2 catalysts synthesized by SCS with a porous γ-Al2O3 support for efficient H2 production via aqueous-phase glycerol reforming</article-title><trans-title-group xml:lang="ru"><trans-title>Ni/CeO2 катализаторы, синтезированные методом растворного горения с использованием пористого носителя γ-Al2O3, для эффективного производства H2 путем водяного риформинга глицерина</trans-title></trans-title-group></title-group><contrib-group><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0001-6689-1430</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Матвеева</surname><given-names>А. Н.</given-names></name><name name-style="western" xml:lang="en"><surname>Matveyeva</surname><given-names>A. N.</given-names></name></name-alternatives><bio xml:lang="en"><p>Anna N. Matveyeva</p><p>Politekhnicheskaya ul., 28, St. Petersburg, 194021</p></bio><email xlink:type="simple">anna.matveyeva@mail.ioffe.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0002-6862-128X</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Омаров</surname><given-names>Ш. О.</given-names></name><name name-style="western" xml:lang="en"><surname>Omarov</surname><given-names>Sh. O.</given-names></name></name-alternatives><bio xml:lang="en"><p>Shamil O. Omarov</p><p>Politekhnicheskaya ul., 28, St. Petersburg, 194021</p></bio><email xlink:type="simple">somarov@mail.ioffe.ru</email><xref ref-type="aff" rid="aff-1"/></contrib><contrib contrib-type="author" corresp="yes"><contrib-id contrib-id-type="orcid">https://orcid.org/0000-0003-2003-0672</contrib-id><name-alternatives><name name-style="eastern" xml:lang="ru"><surname>Теневич</surname><given-names>М. И.</given-names></name><name name-style="western" xml:lang="en"><surname>Tenevich</surname><given-names>M. I.</given-names></name></name-alternatives><bio xml:lang="en"><p>Maksim I. Tenevich</p><p>Politekhnicheskaya ul., 28, St. Petersburg, 194021</p></bio><email xlink:type="simple">m.tenevich@mail.ioffe.ru</email><xref ref-type="aff" rid="aff-1"/></contrib></contrib-group><aff xml:lang="en" id="aff-1"><institution>Ioffe Institute</institution><country>Russian Federation</country></aff><pub-date pub-type="collection"><year>2026</year></pub-date><pub-date pub-type="epub"><day>18</day><month>07</month><year>2026</year></pub-date><volume>17</volume><issue>3</issue><fpage>375</fpage><lpage>386</lpage><permissions><copyright-statement>Copyright &amp;#x00A9; Matveyeva A.N., Omarov S.O., Tenevich M.I., 2026</copyright-statement><copyright-year>2026</copyright-year><copyright-holder xml:lang="ru">Матвеева А.Н., Омаров Ш.О., Теневич М.И.</copyright-holder><copyright-holder xml:lang="en">Matveyeva A.N., Omarov S.O., Tenevich M.I.</copyright-holder><license xml:lang="ru" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>Данная работа распространяется под лицензией Creative Commons Attribution 4.0.</license-p></license><license xml:lang="en" license-type="creative-commons-attribution" xlink:href="https://creativecommons.org/licenses/by/4.0/" xlink:type="simple"><license-p>This work is licensed under a Creative Commons Attribution 4.0 License.</license-p></license></permissions><self-uri xlink:href="https://nanojournal.ifmo.ru/jour/article/view/1845">https://nanojournal.ifmo.ru/jour/article/view/1845</self-uri><abstract><p>Aqueous-phase reforming (APR) of glycerol for H2 production was evaluated over a supported Ni/CeO2 (CeNi) catalyst prepared by introducing a porous γ-Al2O3 support into the reaction mixture during solution combustion synthesis. This approach enables the preparation of a catalyst with improved pore volume and average pore size, which is crucial for facilitating reactant diffusion. Unlike the bulk CeNi system, the presence of alumina increases the availability of active nickel nanoparticles and enhances ceria and nickel dispersion. The glycerol APR results show that CeNi/γ-Al2O3 provides higher glycerol conversion and hydrogen yield compared to the bulk system. Notably, halving the active component content leads to a 2.3-fold increase in activity, which is independent of the feed flow rate and, consequently, of the extent of diffusion limitations. The catalyst obtained in this study outperformed known analogs in terms of H2 formation rate, while maintaining high glycerol conversion and H2 selectivity.</p></abstract><trans-abstract xml:lang="ru"><p>Проведена оценка водяного риформинга глицерина (APR) для получения H2 на Ni/CeO2 (CeNi) катализаторе, полученном путем введения пористого носителя γ-Al2O3 в реакционную смесь в процессе синтеза методом растворного горения. Такой подход позволяет получить катализатор с улучшенным объёмом и средним размером пор, что имеет решающее значение для облегчения диффузии реагентов. В отличие от массивной CeNi системы, присутствие оксида алюминия увеличивает доступность активных наночастиц никеля и улучшает дисперсность оксида церия и никеля. Результаты APR глицерина показывают, что CeNi/γ-Al2O3 обеспечивает большую степень превращения глицерина и выход водорода по сравнению с массивной системой. Примечательно, что уменьшение содержания активного компонента вдвое приводит к 2,3-кратному увеличению активности, которое не зависит от скорости потока исходного сырья и, следовательно, от степени диффузионных ограничений. Полученный в данном исследовании катализатор превзошел известные аналоги по скорости образования H2, сохраняя при этом высокую степень развращения глицерина и селективность по H2.</p></trans-abstract><kwd-group xml:lang="ru"><kwd>никель</kwd><kwd>оксид церия</kwd><kwd>оксид алюминия</kwd><kwd>синтез растворного горения</kwd><kwd>водяной риформинг</kwd><kwd>глицерин</kwd><kwd>водород</kwd></kwd-group><kwd-group xml:lang="en"><kwd>nickel</kwd><kwd>ceria</kwd><kwd>alumina</kwd><kwd>solution combustion synthesis</kwd><kwd>aqueous-phase reforming</kwd><kwd>glycerol</kwd><kwd>hydrogen</kwd></kwd-group><funding-group><funding-statement xml:lang="en">This research was funded by the Russian Science Foundation (grant number 25-7300276, https://rscf.ru/project/25-73-00276/)</funding-statement></funding-group></article-meta></front><back><ref-list><title>References</title><ref id="cit1"><label>1</label><citation-alternatives><mixed-citation xml:lang="ru">Chilakamarry C.R., Sakinah A.M.M., Zularisam A.W., Pandey A. Glycerol waste to value added products and its potential applications. Systems Microbiology and Biomanufacturing, 2021, 1 (4), P. 378–396.</mixed-citation><mixed-citation xml:lang="en">Chilakamarry C.R., Sakinah A.M.M., Zularisam A.W., Pandey A. Glycerol waste to value added products and its potential applications. Systems Microbiology and Biomanufacturing, 2021, 1 (4), P. 378–396.</mixed-citation></citation-alternatives></ref><ref id="cit2"><label>2</label><citation-alternatives><mixed-citation xml:lang="ru">Thompson J.C., He B.B. Characterization of crude glycerol from biodiesel production from multiple feedstocks. Appl. Eng. Agric., 2006, 22 (2), P. 261–265.</mixed-citation><mixed-citation xml:lang="en">Thompson J.C., He B.B. Characterization of crude glycerol from biodiesel production from multiple feedstocks. Appl. Eng. Agric., 2006, 22 (2), P. 261–265.</mixed-citation></citation-alternatives></ref><ref id="cit3"><label>3</label><citation-alternatives><mixed-citation xml:lang="ru">Nomanbhay S., Ong M.Y., Chew K.W., Show P.L., Lam M.K., Chen W.H. Organic carbonate production utilizing crude glycerol derived as by-product of biodiesel production: A review. Energies, 2020, 13 (6), 1483.</mixed-citation><mixed-citation xml:lang="en">Nomanbhay S., Ong M.Y., Chew K.W., Show P.L., Lam M.K., Chen W.H. Organic carbonate production utilizing crude glycerol derived as by-product of biodiesel production: A review. Energies, 2020, 13 (6), 1483.</mixed-citation></citation-alternatives></ref><ref id="cit4"><label>4</label><citation-alternatives><mixed-citation xml:lang="ru">Jitjamnong J., Khongprom P., Ratanawilai T., Ratanawilai S. Techno-economic analysis of glycerol carbonate production by glycerolysis of crude glycerol and urea with multi-functional reactive distillation. Case Studies in Chemical and Environmental Engineering, 2023, 8, 100465.</mixed-citation><mixed-citation xml:lang="en">Jitjamnong J., Khongprom P., Ratanawilai T., Ratanawilai S. Techno-economic analysis of glycerol carbonate production by glycerolysis of crude glycerol and urea with multi-functional reactive distillation. Case Studies in Chemical and Environmental Engineering, 2023, 8, 100465.</mixed-citation></citation-alternatives></ref><ref id="cit5"><label>5</label><citation-alternatives><mixed-citation xml:lang="ru">Matveyeva A.N., Omarov S.O., Gavrilova M.A., Trofimuk A.D., Wa¨rna˚ J., Murzin D.Yu. CeO2-supported Ni and Co catalysts prepared by a solution combustion method for H2 production from glycerol: the effect of fuel/oxidizer ratio and oxygen excess. Catal. Sci. Technol., 2023, 13 (18), P. 5387–5406.</mixed-citation><mixed-citation xml:lang="en">Matveyeva A.N., Omarov S.O., Gavrilova M.A., Trofimuk A.D., Wa¨rna˚ J., Murzin D.Yu. CeO2-supported Ni and Co catalysts prepared by a solution combustion method for H2 production from glycerol: the effect of fuel/oxidizer ratio and oxygen excess. Catal. Sci. Technol., 2023, 13 (18), P. 5387–5406.</mixed-citation></citation-alternatives></ref><ref id="cit6"><label>6</label><citation-alternatives><mixed-citation xml:lang="ru">Roslan N.A., Abidin S.Z., Ideris A., Vo D.V.N. A review on glycerol reforming processes over Ni-based catalyst for hydrogen and syngas productions. Int. J. Hydrogen Energy, 2020, 45 (36), P. 18466–18489.</mixed-citation><mixed-citation xml:lang="en">Roslan N.A., Abidin S.Z., Ideris A., Vo D.V.N. A review on glycerol reforming processes over Ni-based catalyst for hydrogen and syngas productions. Int. J. Hydrogen Energy, 2020, 45 (36), P. 18466–18489.</mixed-citation></citation-alternatives></ref><ref id="cit7"><label>7</label><citation-alternatives><mixed-citation xml:lang="ru">Reynoso A.J., Ayastuy J.L., Iriarte-Velasco U., Gutie´rrez-Ortiz M.A. Aqueous-phase reforming of glycerol over Pt-Co catalyst: Effect of process variables. J. Environ. Chem. Eng., 2022, 10 (3), 107402.</mixed-citation><mixed-citation xml:lang="en">Reynoso A.J., Ayastuy J.L., Iriarte-Velasco U., Gutie´rrez-Ortiz M.A. Aqueous-phase reforming of glycerol over Pt-Co catalyst: Effect of process variables. J. Environ. Chem. Eng., 2022, 10 (3), 107402.</mixed-citation></citation-alternatives></ref><ref id="cit8"><label>8</label><citation-alternatives><mixed-citation xml:lang="ru">Seretis A., Tsiakaras P. A thermodynamic analysis of hydrogen production via aqueous phase reforming of glycerol. Fuel Processing Technology, 2015, 134, P. 107–115.</mixed-citation><mixed-citation xml:lang="en">Seretis A., Tsiakaras P. A thermodynamic analysis of hydrogen production via aqueous phase reforming of glycerol. Fuel Processing Technology, 2015, 134, P. 107–115.</mixed-citation></citation-alternatives></ref><ref id="cit9"><label>9</label><citation-alternatives><mixed-citation xml:lang="ru">Raso R., Abad E., Garc´ıa L., Ruiz J., Oliva M., Arauzo J. Renewable hydrogen production by aqueous phase reforming of pure/refined crude glycerol over Ni/Al–Ca catalysts. Molecules, 2023, 28 (18), 6695.</mixed-citation><mixed-citation xml:lang="en">Raso R., Abad E., Garc´ıa L., Ruiz J., Oliva M., Arauzo J. Renewable hydrogen production by aqueous phase reforming of pure/refined crude glycerol over Ni/Al–Ca catalysts. Molecules, 2023, 28 (18), 6695.</mixed-citation></citation-alternatives></ref><ref id="cit10"><label>10</label><citation-alternatives><mixed-citation xml:lang="ru">Fasolini A., Cespi D., Tabanelli T., Cucciniello R., Cavani F. Hydrogen from renewables: A case study of glycerol reforming. Catalysts, 2019, 9 (9), 722.</mixed-citation><mixed-citation xml:lang="en">Fasolini A., Cespi D., Tabanelli T., Cucciniello R., Cavani F. Hydrogen from renewables: A case study of glycerol reforming. Catalysts, 2019, 9 (9), 722.</mixed-citation></citation-alternatives></ref><ref id="cit11"><label>11</label><citation-alternatives><mixed-citation xml:lang="ru">Coronado I., Stekrova M., Reinikainen M., Simell P., Lefferts L., Lehtonen J. A review of catalytic aqueous-phase reforming of oxygenated hydrocarbons derived from biorefinery water fractions. International Journal of Hydrogen Energy, 2016, 41 (26), P. 11003–11032.</mixed-citation><mixed-citation xml:lang="en">Coronado I., Stekrova M., Reinikainen M., Simell P., Lefferts L., Lehtonen J. A review of catalytic aqueous-phase reforming of oxygenated hydrocarbons derived from biorefinery water fractions. International Journal of Hydrogen Energy, 2016, 41 (26), P. 11003–11032.</mixed-citation></citation-alternatives></ref><ref id="cit12"><label>12</label><citation-alternatives><mixed-citation xml:lang="ru">Liao Y., Wu D., Rezayan A., Zhao J., Xu C. Advances in catalysts for production of renewable H2/CH4 by Aqueous Phase Reforming (APR) of biomass-derived oxygenates. Applications in Energy and Combustion Science, 2025, 24, 100415.</mixed-citation><mixed-citation xml:lang="en">Liao Y., Wu D., Rezayan A., Zhao J., Xu C. Advances in catalysts for production of renewable H2/CH4 by Aqueous Phase Reforming (APR) of biomass-derived oxygenates. Applications in Energy and Combustion Science, 2025, 24, 100415.</mixed-citation></citation-alternatives></ref><ref id="cit13"><label>13</label><citation-alternatives><mixed-citation xml:lang="ru">Cortright R.D., Davda R.R., Dumesic J.A. Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water. Nature, 2002, 418, P. 964–967.</mixed-citation><mixed-citation xml:lang="en">Cortright R.D., Davda R.R., Dumesic J.A. Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water. Nature, 2002, 418, P. 964–967.</mixed-citation></citation-alternatives></ref><ref id="cit14"><label>14</label><citation-alternatives><mixed-citation xml:lang="ru">Manfro R.L., Da Costa A.F., Ribeiro N.F.P., Souza M.M.V.M. Hydrogen production by aqueous-phase reforming of glycerol over nickel catalysts supported on CeO2. Fuel Process. Technol., 2011, 92 (3), P. 330–335.</mixed-citation><mixed-citation xml:lang="en">Manfro R.L., Da Costa A.F., Ribeiro N.F.P., Souza M.M.V.M. Hydrogen production by aqueous-phase reforming of glycerol over nickel catalysts supported on CeO2. Fuel Process. Technol., 2011, 92 (3), P. 330–335.</mixed-citation></citation-alternatives></ref><ref id="cit15"><label>15</label><citation-alternatives><mixed-citation xml:lang="ru">Omarov Sh.O., Martinson K.D., Matveyeva A.N., Chebanenko M.I., Nevedomskiy V.N., Popkov V.I. Renewable hydrogen production via glycerol steam reforming over Ni/CeO2 catalysts obtained by solution combustion method: The effect of Ni loading. Fuel Process. Technol., 2022, 236, 107429.</mixed-citation><mixed-citation xml:lang="en">Omarov Sh.O., Martinson K.D., Matveyeva A.N., Chebanenko M.I., Nevedomskiy V.N., Popkov V.I. Renewable hydrogen production via glycerol steam reforming over Ni/CeO2 catalysts obtained by solution combustion method: The effect of Ni loading. Fuel Process. Technol., 2022, 236, 107429.</mixed-citation></citation-alternatives></ref><ref id="cit16"><label>16</label><citation-alternatives><mixed-citation xml:lang="ru">Cross A., Kumar A., E. Wolf E., S. Mukasyan A. Combustion synthesis of a nickel supported catalyst: Effect of metal distribution on the activity during ethanol decomposition. Ind. Eng. Chem. Res., 2012, 51 (37), P. 12004–12008.</mixed-citation><mixed-citation xml:lang="en">Cross A., Kumar A., E. Wolf E., S. Mukasyan A. Combustion synthesis of a nickel supported catalyst: Effect of metal distribution on the activity during ethanol decomposition. Ind. Eng. Chem. Res., 2012, 51 (37), P. 12004–12008.</mixed-citation></citation-alternatives></ref><ref id="cit17"><label>17</label><citation-alternatives><mixed-citation xml:lang="ru">Cross A., Roslyakov S., Manukyan K. V., Rouvimov S., Rogachev A.S., Kovalev D., Wolf E.E., Mukasyan A.S. In situ preparation of highly stable Ni-based supported catalysts by solution combustion synthesis. J. Phys. Chem. C, 2014, 118 (45), P. 26191–26198.</mixed-citation><mixed-citation xml:lang="en">Cross A., Roslyakov S., Manukyan K. V., Rouvimov S., Rogachev A.S., Kovalev D., Wolf E.E., Mukasyan A.S. In situ preparation of highly stable Ni-based supported catalysts by solution combustion synthesis. J. Phys. Chem. C, 2014, 118 (45), P. 26191–26198.</mixed-citation></citation-alternatives></ref><ref id="cit18"><label>18</label><citation-alternatives><mixed-citation xml:lang="ru">Kumar A., Cross A., Manukyan K., Bhosale R.R., van den Broeke L.J.P., Miller J.T., Mukasyan A.S., Wolf E.E. Combustion synthesis of coppernickel catalysts for hydrogen production from ethanol. Chem. Eng. J., 2015, 278, P. 46–54.</mixed-citation><mixed-citation xml:lang="en">Kumar A., Cross A., Manukyan K., Bhosale R.R., van den Broeke L.J.P., Miller J.T., Mukasyan A.S., Wolf E.E. Combustion synthesis of coppernickel catalysts for hydrogen production from ethanol. Chem. Eng. J., 2015, 278, P. 46–54.</mixed-citation></citation-alternatives></ref><ref id="cit19"><label>19</label><citation-alternatives><mixed-citation xml:lang="ru">Seriyala A.K, Appari S., Roy B. Steam reforming of ethanol for hydrogen production by low-temperature steam reforming using modified NiSn/CeO2 catalyst. Mater. Today Proc., 2022, 76 (2), P. 279–288.</mixed-citation><mixed-citation xml:lang="en">Seriyala A.K, Appari S., Roy B. Steam reforming of ethanol for hydrogen production by low-temperature steam reforming using modified NiSn/CeO2 catalyst. Mater. Today Proc., 2022, 76 (2), P. 279–288.</mixed-citation></citation-alternatives></ref><ref id="cit20"><label>20</label><citation-alternatives><mixed-citation xml:lang="ru">Seriyala A.K., Rao A., Leclerc C., Appari S., Roy B. Effects of metal loading and support modification on the low-temperature steam reforming of ethanol (LTSRE) over the Ni–Sn/CeO2 catalysts. Int. J. Hydrogen Ener., 2023, 48 (41), P. 15533–15554.</mixed-citation><mixed-citation xml:lang="en">Seriyala A.K., Rao A., Leclerc C., Appari S., Roy B. Effects of metal loading and support modification on the low-temperature steam reforming of ethanol (LTSRE) over the Ni–Sn/CeO2 catalysts. Int. J. Hydrogen Ener., 2023, 48 (41), P. 15533–15554.</mixed-citation></citation-alternatives></ref><ref id="cit21"><label>21</label><citation-alternatives><mixed-citation xml:lang="ru">Li J., Tu Y., He K., Chen C., Liang L., Ruan C., Zhang Q. Mechanistic insights into glycerol oxidation to high-value chemicals via metal-based catalysts. Molecules, 2025, 30 (6), 1310.</mixed-citation><mixed-citation xml:lang="en">Li J., Tu Y., He K., Chen C., Liang L., Ruan C., Zhang Q. Mechanistic insights into glycerol oxidation to high-value chemicals via metal-based catalysts. Molecules, 2025, 30 (6), 1310.</mixed-citation></citation-alternatives></ref><ref id="cit22"><label>22</label><citation-alternatives><mixed-citation xml:lang="ru">Sun P., Zhang W., Yu X., Zhang J., Xu N., Zhang Z., Liu M., Zhang D., Zhang G., Liu Z., Yang C., Yan W., Jin X. Hydrogenolysis of glycerol to propylene glycol: Energy, tech-economic, and environmental studies. Front. Chem., 2022, 9, 778579.</mixed-citation><mixed-citation xml:lang="en">Sun P., Zhang W., Yu X., Zhang J., Xu N., Zhang Z., Liu M., Zhang D., Zhang G., Liu Z., Yang C., Yan W., Jin X. Hydrogenolysis of glycerol to propylene glycol: Energy, tech-economic, and environmental studies. Front. Chem., 2022, 9, 778579.</mixed-citation></citation-alternatives></ref><ref id="cit23"><label>23</label><citation-alternatives><mixed-citation xml:lang="ru">Viswanadham N., Saxena S.K. Etherification of glycerol for improved production of oxygenates. Fuel, 2013, 103, P. 980–986.</mixed-citation><mixed-citation xml:lang="en">Viswanadham N., Saxena S.K. Etherification of glycerol for improved production of oxygenates. Fuel, 2013, 103, P. 980–986.</mixed-citation></citation-alternatives></ref><ref id="cit24"><label>24</label><citation-alternatives><mixed-citation xml:lang="ru">Patel A., Singh S. A green and sustainable approach for esterification of glycerol using 12-tungstophosphoric acid anchored to different supports: Kinetics and effect of support. Fuel, 2014, 118, P. 358–364.</mixed-citation><mixed-citation xml:lang="en">Patel A., Singh S. A green and sustainable approach for esterification of glycerol using 12-tungstophosphoric acid anchored to different supports: Kinetics and effect of support. Fuel, 2014, 118, P. 358–364.</mixed-citation></citation-alternatives></ref><ref id="cit25"><label>25</label><citation-alternatives><mixed-citation xml:lang="ru">Maquirriain M.A., Querini C.A., Pisarello M.L. Glycerine esterification with free fatty acids: Homogeneous catalysis. Chemical Engineering Research and Design, 2021, 171, P. 86–99.</mixed-citation><mixed-citation xml:lang="en">Maquirriain M.A., Querini C.A., Pisarello M.L. Glycerine esterification with free fatty acids: Homogeneous catalysis. Chemical Engineering Research and Design, 2021, 171, P. 86–99.</mixed-citation></citation-alternatives></ref><ref id="cit26"><label>26</label><citation-alternatives><mixed-citation xml:lang="ru">Song M., Bai Y., Li J., Qi X. Efficient strategies for the preparation of non-noble metal catalysts for electrocatalytic glycerol oxidation towards high-value-added chemicals. RSC Advances, 2025, 15 (26), P. 20513–20529.</mixed-citation><mixed-citation xml:lang="en">Song M., Bai Y., Li J., Qi X. Efficient strategies for the preparation of non-noble metal catalysts for electrocatalytic glycerol oxidation towards high-value-added chemicals. RSC Advances, 2025, 15 (26), P. 20513–20529.</mixed-citation></citation-alternatives></ref><ref id="cit27"><label>27</label><citation-alternatives><mixed-citation xml:lang="ru">Lotfi M., Esmaeilnejad-Ahranjani P. New insights into controlling rapid combustion synthesis procedure: Shape-tailored Fe3O4 nanoparticles fabrication. J. Magn. Magn. Mater., 2024, 603, 172252.</mixed-citation><mixed-citation xml:lang="en">Lotfi M., Esmaeilnejad-Ahranjani P. New insights into controlling rapid combustion synthesis procedure: Shape-tailored Fe3O4 nanoparticles fabrication. J. Magn. Magn. Mater., 2024, 603, 172252.</mixed-citation></citation-alternatives></ref><ref id="cit28"><label>28</label><citation-alternatives><mixed-citation xml:lang="ru">Voskanyan A.A., Chan K.-Y., Li C.-Y.V. Colloidal solution combustion synthesis: Toward mass production of a crystalline uniform mesoporous CeO2 catalyst with tunable porosity. Chem. Mater., American Chemical Society, 2016, 28 (8), P. 2768–2775.</mixed-citation><mixed-citation xml:lang="en">Voskanyan A.A., Chan K.-Y., Li C.-Y.V. Colloidal solution combustion synthesis: Toward mass production of a crystalline uniform mesoporous CeO2 catalyst with tunable porosity. Chem. Mater., American Chemical Society, 2016, 28 (8), P. 2768–2775.</mixed-citation></citation-alternatives></ref><ref id="cit29"><label>29</label><citation-alternatives><mixed-citation xml:lang="ru">Matveyeva A.N., Omarov S.O. Comparison of Perovskite Systems Based on AFeO3 (A = Ce, La, Y) in CO2 Hydrogenation to CO. Transactions of Tianjin University, 2024, 30 (4), P. 337–358.</mixed-citation><mixed-citation xml:lang="en">Matveyeva A.N., Omarov S.O. Comparison of Perovskite Systems Based on AFeO3 (A = Ce, La, Y) in CO2 Hydrogenation to CO. Transactions of Tianjin University, 2024, 30 (4), P. 337–358.</mixed-citation></citation-alternatives></ref><ref id="cit30"><label>30</label><citation-alternatives><mixed-citation xml:lang="ru">Matveyeva A.N., Omarov S.O., Gavrilova M.A. Alumina and silica supported Ce–Fe–O systems obtained by the solution combustion method and their performance in CO2 hydrogenation to syngas. Nanosyst.: Phys. Chem. Math., 2023, 14 (6), P. 679–689.</mixed-citation><mixed-citation xml:lang="en">Matveyeva A.N., Omarov S.O., Gavrilova M.A. Alumina and silica supported Ce–Fe–O systems obtained by the solution combustion method and their performance in CO2 hydrogenation to syngas. Nanosyst.: Phys. Chem. Math., 2023, 14 (6), P. 679–689.</mixed-citation></citation-alternatives></ref><ref id="cit31"><label>31</label><citation-alternatives><mixed-citation xml:lang="ru">Omarov Sh.O., Sladkovskiy D.A., Martinson K.D., Peurla M., Aho A., Murzin D.Yu., Popkov V.I. Influence of the initial state of ZrO2 on genesis, activity and stability of Ni/ZrO2 catalysts for steam reforming of glycerol. Appl. Catal. A Gen., 2021, 616, 118098.</mixed-citation><mixed-citation xml:lang="en">Omarov Sh.O., Sladkovskiy D.A., Martinson K.D., Peurla M., Aho A., Murzin D.Yu., Popkov V.I. Influence of the initial state of ZrO2 on genesis, activity and stability of Ni/ZrO2 catalysts for steam reforming of glycerol. Appl. Catal. A Gen., 2021, 616, 118098.</mixed-citation></citation-alternatives></ref><ref id="cit32"><label>32</label><citation-alternatives><mixed-citation xml:lang="ru">Egoburo D.E., Diaz Pen˜a R., Kolender A., Pettinari M.J. Optimization and validation of a GC–FID method for quantitative determination of 1,3-propanediol in bacterial culture aqueous supernatants containing glycerol. Chromatographia, 2017, 80 (7), P. 1121–1127.</mixed-citation><mixed-citation xml:lang="en">Egoburo D.E., Diaz Pen˜a R., Kolender A., Pettinari M.J. Optimization and validation of a GC–FID method for quantitative determination of 1,3-propanediol in bacterial culture aqueous supernatants containing glycerol. Chromatographia, 2017, 80 (7), P. 1121–1127.</mixed-citation></citation-alternatives></ref><ref id="cit33"><label>33</label><citation-alternatives><mixed-citation xml:lang="ru">Ahmad N., Alam M., Wahab R., Ahmad J., Ubaidullah M., Ansari A.A., Alotaibi N.M. Synthesis of NiO–CeO2 nanocomposite for electrochemical sensing of perilous 4-nitrophenol. Journal of Materials Science: Materials in Electronics, 2019, 30 (19), P. 17643–17653.</mixed-citation><mixed-citation xml:lang="en">Ahmad N., Alam M., Wahab R., Ahmad J., Ubaidullah M., Ansari A.A., Alotaibi N.M. Synthesis of NiO–CeO2 nanocomposite for electrochemical sensing of perilous 4-nitrophenol. Journal of Materials Science: Materials in Electronics, 2019, 30 (19), P. 17643–17653.</mixed-citation></citation-alternatives></ref><ref id="cit34"><label>34</label><citation-alternatives><mixed-citation xml:lang="ru">Jayakumar G., Irudayaraj A.A., Raj A.D. Investigation on the synthesis and photocatalytic activity of activated carbon–cerium oxide (AC–CeO2) nanocomposite. Appl. Phys. A Mater. Sci. Process., 2019, 125 (11), 742.</mixed-citation><mixed-citation xml:lang="en">Jayakumar G., Irudayaraj A.A., Raj A.D. Investigation on the synthesis and photocatalytic activity of activated carbon–cerium oxide (AC–CeO2) nanocomposite. Appl. Phys. A Mater. Sci. Process., 2019, 125 (11), 742.</mixed-citation></citation-alternatives></ref><ref id="cit35"><label>35</label><citation-alternatives><mixed-citation xml:lang="ru">Ravishankar T.N., Ramakrishnappa T., Nagaraju G., Rajanaika H. Synthesis and characterization of CeO2 nanoparticles via solution combustion method for photocatalytic and antibacterial activity studies. Chemistry Open, 2015, 4 (2), P. 146–154.</mixed-citation><mixed-citation xml:lang="en">Ravishankar T.N., Ramakrishnappa T., Nagaraju G., Rajanaika H. Synthesis and characterization of CeO2 nanoparticles via solution combustion method for photocatalytic and antibacterial activity studies. Chemistry Open, 2015, 4 (2), P. 146–154.</mixed-citation></citation-alternatives></ref><ref id="cit36"><label>36</label><citation-alternatives><mixed-citation xml:lang="ru">Romero Toledo R., Ruiz Santoyo V., Moncada Sa´nchez C.D., Mart´ınes Rosales M. Effect of aluminum precursor on physicochemical properties of Al2O3 by hydrolysis/precipitation method. Nova Scientia, 2018, 10 (20), P. 83–99.</mixed-citation><mixed-citation xml:lang="en">Romero Toledo R., Ruiz Santoyo V., Moncada Sa´nchez C.D., Mart´ınes Rosales M. Effect of aluminum precursor on physicochemical properties of Al2O3 by hydrolysis/precipitation method. Nova Scientia, 2018, 10 (20), P. 83–99.</mixed-citation></citation-alternatives></ref><ref id="cit37"><label>37</label><citation-alternatives><mixed-citation xml:lang="ru">Asencios Y.J.O., Sun-Kou M.R. Synthesis of high-surface-area γ-Al2O3 from aluminum scrap and its use for the adsorption of metals: Pb(II), Cd(II) and Zn(II). Appl. Surf. Sci., 2012, 258 (24), P. 10002–10011.</mixed-citation><mixed-citation xml:lang="en">Asencios Y.J.O., Sun-Kou M.R. Synthesis of high-surface-area γ-Al2O3 from aluminum scrap and its use for the adsorption of metals: Pb(II), Cd(II) and Zn(II). Appl. Surf. Sci., 2012, 258 (24), P. 10002–10011.</mixed-citation></citation-alternatives></ref><ref id="cit38"><label>38</label><citation-alternatives><mixed-citation xml:lang="ru">Cheng C.K., Foo S.Y., Adesina A.A. Steam reforming of glycerol over Ni/Al2O3 catalyst. Catal. Today, 2011, 178 (1), P. 25–33.</mixed-citation><mixed-citation xml:lang="en">Cheng C.K., Foo S.Y., Adesina A.A. Steam reforming of glycerol over Ni/Al2O3 catalyst. Catal. Today, 2011, 178 (1), P. 25–33.</mixed-citation></citation-alternatives></ref><ref id="cit39"><label>39</label><citation-alternatives><mixed-citation xml:lang="ru">Song F., Zhong Q., Yu Y., Shi M., Wu Y., Hu J., Song Y. Obtaining well-dispersed Ni/Al2O3 catalyst for CO2 methanation with a microwaveassisted method. Int. J. Hydrogen Energy, 2017, 42 (7), P. 4174–4183.</mixed-citation><mixed-citation xml:lang="en">Song F., Zhong Q., Yu Y., Shi M., Wu Y., Hu J., Song Y. Obtaining well-dispersed Ni/Al2O3 catalyst for CO2 methanation with a microwaveassisted method. Int. J. Hydrogen Energy, 2017, 42 (7), P. 4174–4183.</mixed-citation></citation-alternatives></ref><ref id="cit40"><label>40</label><citation-alternatives><mixed-citation xml:lang="ru">Wang N., Xu Z., Deng J., Shen K., Yu X., Qian W., Chu W., Wei F. One-pot synthesis of ordered mesoporous NiCeAl oxide catalysts and a study of their performance in methane dry reforming. ChemCatChem, 2014, 6 (5), P. 1470–1480.</mixed-citation><mixed-citation xml:lang="en">Wang N., Xu Z., Deng J., Shen K., Yu X., Qian W., Chu W., Wei F. One-pot synthesis of ordered mesoporous NiCeAl oxide catalysts and a study of their performance in methane dry reforming. ChemCatChem, 2014, 6 (5), P. 1470–1480.</mixed-citation></citation-alternatives></ref><ref id="cit41"><label>41</label><citation-alternatives><mixed-citation xml:lang="ru">Sangsong S., Ratana T., Tungkamani S., Sornchamni T., Phongaksorn M. Effect of CeO2 loading of the Ce-Al mixed oxide on ultrahigh temperature water-gas shift performance over Ce–Al mixed oxide supported Ni catalysts. Fuel, 2019, 252, P. 488–495.</mixed-citation><mixed-citation xml:lang="en">Sangsong S., Ratana T., Tungkamani S., Sornchamni T., Phongaksorn M. Effect of CeO2 loading of the Ce-Al mixed oxide on ultrahigh temperature water-gas shift performance over Ce–Al mixed oxide supported Ni catalysts. Fuel, 2019, 252, P. 488–495.</mixed-citation></citation-alternatives></ref><ref id="cit42"><label>42</label><citation-alternatives><mixed-citation xml:lang="ru">Yang L., Pastor-Pe´rez L., Gu S., Sepu´lveda-Escribano A., Reina T.R. Highly efficient Ni/CeO2-Al2O3 catalysts for CO2 upgrading via reverse water-gas shift: Effect of selected transition metal promoters. Appl. Catal. B, 2018, 232, P. 464–471.</mixed-citation><mixed-citation xml:lang="en">Yang L., Pastor-Pe´rez L., Gu S., Sepu´lveda-Escribano A., Reina T.R. Highly efficient Ni/CeO2-Al2O3 catalysts for CO2 upgrading via reverse water-gas shift: Effect of selected transition metal promoters. Appl. Catal. B, 2018, 232, P. 464–471.</mixed-citation></citation-alternatives></ref><ref id="cit43"><label>43</label><citation-alternatives><mixed-citation xml:lang="ru">Santos D. dos S., Rolda˜o C.P., Gelesky M.A., Pacheco H., Mortola V.B. Synthesis Strategies for the Optimization of Ni–Ce–Al Catalysts in the Conversion of CO2 to Methanol. Ind. Eng. Chem. Res., 2025, 64 (52), P. 24925–24937.</mixed-citation><mixed-citation xml:lang="en">Santos D. dos S., Rolda˜o C.P., Gelesky M.A., Pacheco H., Mortola V.B. Synthesis Strategies for the Optimization of Ni–Ce–Al Catalysts in the Conversion of CO2 to Methanol. Ind. Eng. Chem. Res., 2025, 64 (52), P. 24925–24937.</mixed-citation></citation-alternatives></ref><ref id="cit44"><label>44</label><citation-alternatives><mixed-citation xml:lang="ru">He L., Ren Y., Yue B., Tsang S.C.E., He H. Tuning metal–support interactions on Ni/Al2O3 catalysts to improve catalytic activity and stability for dry reforming of methane. Processes, 2021, 9 (4), 706.</mixed-citation><mixed-citation xml:lang="en">He L., Ren Y., Yue B., Tsang S.C.E., He H. Tuning metal–support interactions on Ni/Al2O3 catalysts to improve catalytic activity and stability for dry reforming of methane. Processes, 2021, 9 (4), 706.</mixed-citation></citation-alternatives></ref><ref id="cit45"><label>45</label><citation-alternatives><mixed-citation xml:lang="ru">Mierczynski P., Mierczynska A., Ciesielski R., Mosinska M., Nowosielska M., Czylkowska A., Maniukiewicz W., Szynkowska M.I., Vasilev K. High active and selective Ni/CeO2-Al2O3 and Pd–Ni/CeO2–Al2O3 catalysts for oxy-steam reforming of methanol. Catalysts, 2018, 8 (9), 380.</mixed-citation><mixed-citation xml:lang="en">Mierczynski P., Mierczynska A., Ciesielski R., Mosinska M., Nowosielska M., Czylkowska A., Maniukiewicz W., Szynkowska M.I., Vasilev K. High active and selective Ni/CeO2-Al2O3 and Pd–Ni/CeO2–Al2O3 catalysts for oxy-steam reforming of methanol. Catalysts, 2018, 8 (9), 380.</mixed-citation></citation-alternatives></ref><ref id="cit46"><label>46</label><citation-alternatives><mixed-citation xml:lang="ru">Vacharapong P., Arayawate S., Katanyutanon S., Toochinda P., Lawtrakul L., Charojrochkul S. Enhancement of Ni catalyst using CeO2-Al2O3 support prepared with magnetic inducement for ESR. Catalysts, 2020, 10 (11), 1357.</mixed-citation><mixed-citation xml:lang="en">Vacharapong P., Arayawate S., Katanyutanon S., Toochinda P., Lawtrakul L., Charojrochkul S. Enhancement of Ni catalyst using CeO2-Al2O3 support prepared with magnetic inducement for ESR. Catalysts, 2020, 10 (11), 1357.</mixed-citation></citation-alternatives></ref><ref id="cit47"><label>47</label><citation-alternatives><mixed-citation xml:lang="ru">Lee H.-J., Shin G.S., Kim Y.-C. Characterization of supported Ni catalysts for aqueous-phase reforming of glycerol. Korean J. Chem. Eng., 2015, 32 (7), 1267–1272.</mixed-citation><mixed-citation xml:lang="en">Lee H.-J., Shin G.S., Kim Y.-C. Characterization of supported Ni catalysts for aqueous-phase reforming of glycerol. Korean J. Chem. Eng., 2015, 32 (7), 1267–1272.</mixed-citation></citation-alternatives></ref><ref id="cit48"><label>48</label><citation-alternatives><mixed-citation xml:lang="ru">Park J.H., Lu H., Sharma B.K., Johnston D., Rajagopalan N., Kim J. Regenerable oxygen-deficient Ni/γ-Al2O3 catalyst for efficient glycerol aqueous phase reforming. J. Mater. Chem. A, 2025, P. 3449–3460.</mixed-citation><mixed-citation xml:lang="en">Park J.H., Lu H., Sharma B.K., Johnston D., Rajagopalan N., Kim J. Regenerable oxygen-deficient Ni/γ-Al2O3 catalyst for efficient glycerol aqueous phase reforming. J. Mater. Chem. A, 2025, P. 3449–3460.</mixed-citation></citation-alternatives></ref><ref id="cit49"><label>49</label><citation-alternatives><mixed-citation xml:lang="ru">Morales-Mar´ın A., Iriarte-Velasco U., Gutie´rrez-Ortiz M.A´ ., Ayastuy J.L. Aqueous-phase glycerol conversion over Ni-based catalysts synthesized by nanocasting. Catalysts, 2022, 12 (6), 668.</mixed-citation><mixed-citation xml:lang="en">Morales-Mar´ın A., Iriarte-Velasco U., Gutie´rrez-Ortiz M.A´ ., Ayastuy J.L. Aqueous-phase glycerol conversion over Ni-based catalysts synthesized by nanocasting. Catalysts, 2022, 12 (6), 668.</mixed-citation></citation-alternatives></ref><ref id="cit50"><label>50</label><citation-alternatives><mixed-citation xml:lang="ru">Alessio H.J., Pestana G.L., Comelli R.A., Grau J.M. Hydrogen production via aqueous phase reforming of glycerol over Ni-Co/γ-Al2O3 catalysts: Effect of support modification with lanthanides and alkaline earth metals. Fuel, 2026, 404, 136217.</mixed-citation><mixed-citation xml:lang="en">Alessio H.J., Pestana G.L., Comelli R.A., Grau J.M. Hydrogen production via aqueous phase reforming of glycerol over Ni-Co/γ-Al2O3 catalysts: Effect of support modification with lanthanides and alkaline earth metals. Fuel, 2026, 404, 136217.</mixed-citation></citation-alternatives></ref><ref id="cit51"><label>51</label><citation-alternatives><mixed-citation xml:lang="ru">Yarbas¸ T., Ayas N. A detailed thermodynamic analysis of CO2 hydrogenation to produce methane at low pressure. Int. J. Hydrogen Energy, Pergamon, 2024, 49, P. 1134–1144.</mixed-citation><mixed-citation xml:lang="en">Yarbas¸ T., Ayas N. A detailed thermodynamic analysis of CO2 hydrogenation to produce methane at low pressure. Int. J. Hydrogen Energy, Pergamon, 2024, 49, P. 1134–1144.</mixed-citation></citation-alternatives></ref><ref id="cit52"><label>52</label><citation-alternatives><mixed-citation xml:lang="ru">Bazghaleh F.S., Darian J.T., Niktab Y., Yazd M.S. A comprehensive thermodynamic equilibrium analysis of direct CO2 hydrogenation to light olefins product. Journal of CO2 Utilization, 2025, 102, 103238.</mixed-citation><mixed-citation xml:lang="en">Bazghaleh F.S., Darian J.T., Niktab Y., Yazd M.S. A comprehensive thermodynamic equilibrium analysis of direct CO2 hydrogenation to light olefins product. Journal of CO2 Utilization, 2025, 102, 103238.</mixed-citation></citation-alternatives></ref><ref id="cit53"><label>53</label><citation-alternatives><mixed-citation xml:lang="ru">Kee C.W., Zheng J., Yap W.J., Ou Yong R., Liu Y. Thermal and sono – aqueous reforming of alcohols for sustainable hydrogen production. Molecules, 2024, 29 (20), 4867.</mixed-citation><mixed-citation xml:lang="en">Kee C.W., Zheng J., Yap W.J., Ou Yong R., Liu Y. Thermal and sono – aqueous reforming of alcohols for sustainable hydrogen production. Molecules, 2024, 29 (20), 4867.</mixed-citation></citation-alternatives></ref></ref-list><fn-group><fn fn-type="conflict"><p>The authors declare that there are no conflicts of interest present.</p></fn></fn-group></back></article>
