TY - JOUR
T1 - A comparative study of SiO2, Al2O3, and mixed SiO2-Al2O3-supported nickel catalysts for dry reforming of methane
T2 - effects of calcination temperature on catalytic performance
AU - Alshammari, Dalal A.
AU - Aladeemy, Saba A.
AU - Ali, Rehab M.
AU - Marouani, Maryam El
AU - El-Naggar, Naglaa A.
AU - Alharbi, Fawaz S.
AU - Alsayed, Abdullah A.
AU - Ibrahim, Ahmed A.
AU - Al-Fatesh, Ahmed S.
N1 - Publisher Copyright:
© The Author(s), under exclusive licence to Springer Science+Business Media, LLC, part of Springer Nature 2025.
PY - 2026/1
Y1 - 2026/1
N2 - Dry reforming of methane (DRM) offers a sustainable approach for the simultaneous utilization of two major greenhouse gases (CH4 and CO2) to generate synthesis gas (syngas). In this study, a comparative investigation of Ni catalysts supported on SiO2 (Si), Al2O3 (Al), and mixed SiO2-Al2O3 (3.5Si + Al) was conducted to assess the effect of calcination temperature on catalyst structure–activity relationships. Catalysts were synthesized via wet impregnation and calcined at 600 °C and 800 °C, followed by extensive characterization using N2 physisorption, XRD, H₂-TPR, CO₂-TPD, TGA, Raman spectroscopy, and TEM to examine their physicochemical properties before and after reaction. Catalytic performance was evaluated by monitoring CH4 and CO2 conversions under controlled DRM conditions. The results demonstrated that 5Ni/Si catalysts exhibited weak basicity and unstable active sites, limiting DRM performance irrespective of calcination temperature. In contrast, catalysts supported on Al2O3 and mixed SiO2-Al2O3 and calcined at 600 °C showed higher catalytic activity, attributed to stronger metal–support interactions and the formation of stable active sites. Specifically, 5Ni/Al and 5Ni/(3.5Si + Al) catalysts achieved ~ 58% CH4 conversion and ~ 65–66% CO2 conversion over 375 min on stream. However, calcination of 5Ni/(3.5Si + Al) at 800 °C resulted in a significant decrease in the number of active sites at 700 °C reduction/reaction temperature, leading to severe loss of catalytic activity. Further analysis of the best catalyst displayed that increasing the reaction temperature from 700 °C to 800 °C positively affected both CH4 and CO2 conversions and the H2/CO ratio while increasing the space velocity made every parameter worse. The stability test at 700 °C showed that it was stable for 20 h. Hence, this work highlights the importance of support composition and thermal treatment in tailoring the structural and catalytic properties of Ni-based catalysts. The findings provide valuable insights for designing efficient, stable catalysts for syngas production via DRM, contributing to greenhouse gas mitigation through carbon utilization technologies.
AB - Dry reforming of methane (DRM) offers a sustainable approach for the simultaneous utilization of two major greenhouse gases (CH4 and CO2) to generate synthesis gas (syngas). In this study, a comparative investigation of Ni catalysts supported on SiO2 (Si), Al2O3 (Al), and mixed SiO2-Al2O3 (3.5Si + Al) was conducted to assess the effect of calcination temperature on catalyst structure–activity relationships. Catalysts were synthesized via wet impregnation and calcined at 600 °C and 800 °C, followed by extensive characterization using N2 physisorption, XRD, H₂-TPR, CO₂-TPD, TGA, Raman spectroscopy, and TEM to examine their physicochemical properties before and after reaction. Catalytic performance was evaluated by monitoring CH4 and CO2 conversions under controlled DRM conditions. The results demonstrated that 5Ni/Si catalysts exhibited weak basicity and unstable active sites, limiting DRM performance irrespective of calcination temperature. In contrast, catalysts supported on Al2O3 and mixed SiO2-Al2O3 and calcined at 600 °C showed higher catalytic activity, attributed to stronger metal–support interactions and the formation of stable active sites. Specifically, 5Ni/Al and 5Ni/(3.5Si + Al) catalysts achieved ~ 58% CH4 conversion and ~ 65–66% CO2 conversion over 375 min on stream. However, calcination of 5Ni/(3.5Si + Al) at 800 °C resulted in a significant decrease in the number of active sites at 700 °C reduction/reaction temperature, leading to severe loss of catalytic activity. Further analysis of the best catalyst displayed that increasing the reaction temperature from 700 °C to 800 °C positively affected both CH4 and CO2 conversions and the H2/CO ratio while increasing the space velocity made every parameter worse. The stability test at 700 °C showed that it was stable for 20 h. Hence, this work highlights the importance of support composition and thermal treatment in tailoring the structural and catalytic properties of Ni-based catalysts. The findings provide valuable insights for designing efficient, stable catalysts for syngas production via DRM, contributing to greenhouse gas mitigation through carbon utilization technologies.
UR - https://www.scopus.com/pages/publications/105024604522
U2 - 10.1007/s10853-025-11935-x
DO - 10.1007/s10853-025-11935-x
M3 - Article
AN - SCOPUS:105024604522
SN - 0022-2461
VL - 61
SP - 834
EP - 853
JO - Journal of Materials Science
JF - Journal of Materials Science
IS - 2
ER -