The methane emission from natural sources cannot be stopped and it makes the global warming situation worse. Hope lies in its catalytic conversion into useful ‘syngas’ in the presence of oxygen and this reaction is partial oxidation of methane (POM). A mordenite-type molecular sieve having silica-alumina ratio 20 (abbreviated as CBV20A) is investigated herein to stabilize the active sites Ni at their cages and charge compensation sites. The promotion role of ceria over 5Ni/ CBV20A is further investigated to improve the catalytic performance towards POM. The catalyst’s texture property, crystallinity, polarizability, adsorption-desorption-oxidation and topology are studied by surface area-porosity, X-ray diffraction study, Raman spectroscopy, temperature programmed techniques and transmission electron microscopy respectively. The metal-support interaction is enhanced by the periodic exposure of hydrogen and oxygen during POM over the current catalyst system. Upon promotional addition of 2wt% ceria over Ni/CBV20A, the concentration of active sites are growing, the weak metal-support interaction diminished and strong metal-support established. The surface area and pore volume of this catalyst is also greater than those of the rest of the catalyst. The improved reduction profile and surface texture property turns 2 wt.% ceria promoted 5Ni/ CBV20A catalyst best towards POM reaction. It catalyzes POM gas feed composed of 50% CH4, 25% O2, and 25% N2 (total space velocity14400 mL/h/gcat) most effectively and achieves 62% H2 yield with H2/CO ratio of 2.5 during 230 min time on stream and ~60% H2 yield with H2/CO ratio of 2.4 during 22 h time on stream at 650 °C. High catalytic activity and the generation of hydrogen-rich syngas demonstrate the potential of Ni-based catalysts supported on a molecular sieve with a Ce promoter for POM.
