Ni/CeO2 catalysts synthesized by SCS with a porous γ-Al2O3 support for efficient H2 production via aqueous-phase glycerol reforming
https://doi.org/10.17586/2220-8054-2026-17-3-375-386
Abstract
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.
Keywords
About the Authors
A. N. MatveyevaRussian Federation
Anna N. Matveyeva
Politekhnicheskaya ul., 28, St. Petersburg, 194021
Sh. O. Omarov
Russian Federation
Shamil O. Omarov
Politekhnicheskaya ul., 28, St. Petersburg, 194021
M. I. Tenevich
Russian Federation
Maksim I. Tenevich
Politekhnicheskaya ul., 28, St. Petersburg, 194021
References
1. 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.
2. 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.
3. 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.
4. 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.
5. 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.
6. 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.
7. 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.
8. Seretis A., Tsiakaras P. A thermodynamic analysis of hydrogen production via aqueous phase reforming of glycerol. Fuel Processing Technology, 2015, 134, P. 107–115.
9. 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.
10. Fasolini A., Cespi D., Tabanelli T., Cucciniello R., Cavani F. Hydrogen from renewables: A case study of glycerol reforming. Catalysts, 2019, 9 (9), 722.
11. 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.
12. 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.
13. 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.
14. 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.
15. 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.
16. 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.
17. 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.
18. 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.
19. 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.
20. 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.
21. 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.
22. 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.
23. Viswanadham N., Saxena S.K. Etherification of glycerol for improved production of oxygenates. Fuel, 2013, 103, P. 980–986.
24. 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.
25. 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.
26. 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.
27. 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.
28. 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.
29. 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.
30. 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.
31. 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.
32. 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.
33. 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.
34. 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.
35. 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.
36. 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.
37. 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.
38. 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.
39. 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.
40. 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.
41. 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.
42. 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.
43. 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.
44. 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.
45. 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.
46. 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.
47. 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.
48. 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.
49. 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.
50. 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.
51. 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.
52. 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.
53. 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.
Review
For citations:
Matveyeva A.N., Omarov Sh.O., Tenevich M.I. Ni/CeO2 catalysts synthesized by SCS with a porous γ-Al2O3 support for efficient H2 production via aqueous-phase glycerol reforming. Nanosystems: Physics, Chemistry, Mathematics. 2026;17(3):375-386. https://doi.org/10.17586/2220-8054-2026-17-3-375-386
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