Sol-gel synthesis of Ni and Ni supported catalysts for hydrogen production by methane decomposition

NiO, NiO-CuO, NiO-TiO2 and NiO-CeO2 were synthesized by the sol-gel method and further processed into catalysts for hydrogen production by the thermocatalytic decomposition of methane. The structures of the metal oxides and catalysts were extensively characterized by transmission electron microscopy, X-ray diffraction, energy dispersive X-ray spectroscopy, X-ray photoelectron spectroscopy, temperature-programmed reduction and N-2 adsorption. The catalytic performance of the catalysts was evaluated in terms of methane conversion and carbon yield. NiO had a BET surface area of 66 m(2) g(-1). When compared with NiO, NiO-CuO had a lower BET surface area of 13 m(2) g(-1), while NiO-TiO2 and NiO-CeO2 had higher BET surface areas of 161 and 133 m(2) g(-1), respectively. The resulting supported catalysts required increased reduction temperatures and had higher Ni 2p(3/2) binding energies, indicating strong metal-support interactions. For the Ni-Cu catalyst, the introduction of copper resulted in a lower Ni 2p(3/2) binding energy due to the charge transfer from Cu to the adjacent Ni atoms. The Ni catalyst showed a stable methane conversion of 0.39 at 550 degrees C. The presence of copper in the Ni-Cu catalyst increased the working temperature but decreased methane conversion. The Ni-TiO2 and Ni-CeO2 catalysts exhibited stable methane conversions of 0.56 and 0.60, respectively, at 575 degrees C. The lifetime tests of the catalysts revealed that the Ni catalyst had a life span of 600 min at 550 degrees C, resulting in a carbon yield of 121 g C per g Ni. The Ni-Cu, Ni-CeO2 and Ni-TiO2 catalysts had life spans of 670, 790 and 840 min at 575 degrees C, resulting in carbon yields of 171, 204 and 256 g C per g Ni, respectively. The structures of the resulting carbon products were characterized by transmission electron microscopy and X-ray diffraction. It was found that the morphologies of the resulting carbon products were dependent on the type of catalyst used.