Exploring enhanced syngas production via the catalytic performance of metal-doped X-Ni/CeO2 (X = Zr, La, Sr) in the dry reforming of methane

Background

The quest to manufacture large amounts of syngas to bridge fossil fuels and the renewable energy ecosystem stimulates the creation of efficient and stable heterogeneous catalysts. The NiCeO₂ catalysts, synthesized via ultrasonic-assisted citric acid complexation, are highly efficient for the dry reforming of methane (DRM) reaction. Different promoter metals (Zr, La and Sr) were tested for catalytic performance and syngas production. A range of analyses, including X-ray diffraction (XRD), N₂ physisorption, H₂ temperature-programmed reduction, CO₂ temperature-programmed desorption, field emission scanning electron microscopy (FESEM), transmission electron microscopy and X-ray photoelectron spectroscopy, were employed to characterize the physicochemical properties of the catalysts.

Results

XRD results indicated the formation of NiO, CeO₂, solid solution ceria–zirconia, perovskite LaNiO₃ and SrNiO₃ crystalline phases. FESEM results showed the promoted catalysts (Zr, La, Sr) produce large pores to facilitate reactant diffusion, with zirconia specifically creating a spiderweb morphology. At 800 °C, the CH₄ and CO₂ conversions follow the sequence of NiCeO₂ catalyst (CH₄ = 54%, CO₂ = 45%) < Sr/NiCeO₂ (CH₄ = 60%, CO₂ = 67%) < La/NiCeO₂ (CH₄ = 85%, CO₂ = 84%) < Zr/NiCeO₂ (CH₄ = 95%, CO₂ = 87%). The integration of promoters in DRM catalysts has notably improved carbon formation resistance, as evidenced by the following ranking: Zr/NiCeO₂ (5.1 wt%) < commercial catalyst (6.0 wt%) < La/NiCeO₂ (7.85 wt%) < Sr/NiCeO₂ (10.9 wt%) < NiCeO₂ (11.3 wt%).

Conclusion

This study demonstrates that incorporating promoters, particularly Zr, in NiCeO₂ significantly enhances resistance to carbon formation. It offers valuable insights into selecting metal catalyst promoters for excellent catalytic performance in DRM. © 2024 Society of Chemical Industry (SCI).