Abstract
Natural emissions of the highly potent greenhouse gas methane cannot be completely prevented, but in the presence of O2, methane can be catalytically converted to hydrogen-rich syngas. This reaction is specified as partial oxidation of methane (POM). Herein, Ni dispersed over “scandia-stabilized-zirconia” (5Ni/DSZ) and the promotional effect of Pd (0.01 to 0.1 wt%) are investigated for POM and characterized with surface area and porosity measurements, X-ray diffraction, Raman spectroscopy, temperature-programmed studies, and thermogravimetry. During the POM, the initial population of active Ni sites decreases in non-promoted catalysts due to oxidation under oxygen, upon loading of 0.02 wt.% Pd over 5Ni/DSZ, the active site population is preserved against oxygen during the POM due to improved metal support interaction between Ni and long-range order crystallites of support (like cubic ZrO2 and orthorhombic Sc2Zr5O13). 5Ni0.02 Pd/DSZ catalyst acquired more than 80% catalytic activity (CH4 conversion and H2 yield) with 2.5 H2/CO ratio at 600°C during 240 min on stream. The 5Ni0.02 Pd/DSZ catalyst also maintained more than 70% H2 yield with H2/CO ratio ~2 during 30 h time on stream. The thermostable 5Ni0.02 Pd/DSZ catalyst may be recommended for hydrogen-rich syngas production with high H2-yield through POM.
Original language | English |
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Pages (from-to) | 3935-3944 |
Number of pages | 10 |
Journal | Energy Science and Engineering |
Volume | 13 |
Issue number | 8 |
DOIs | |
State | Published - Aug 2025 |
Keywords
- Ni catalyst
- POM
- Pd-promoter
- crystallinity
- reducibility
- scandia-stabilized-zirconia