Abstract

NiO–TiO 2/WO 3 catalysts was prepared by drying powdered Ni(OH) 2–Ti(OH) 4 with ammonium metatungstate aqueous solution, followed by calcining in air at high temperature. The presence of NiO and WO 3 prevented the phase transition of TiO 2 from anatase to rutile forms. From 600 °C of calcination temperature, nickel titanium oxide (NiTiO 3) was observed due to the reaction between TiO 2 and NiO; its amount increased with increasing calcination temperature. Upon the addition of tungsten oxide to titania up to 15 wt.%, the specific surface area and acidity of catalysts increased in proportion to the tungsten oxide content, due to the interaction between tungsten oxide and titania. Since the TiO 2 stabilizes the tungsten oxide species, for the samples equal to or less than 25 wt.%, tungsten oxide was well dispersed on the surface of titania, but for the samples containing 25 wt.% or above 25 wt.%, the triclinic phase of WO 3 was observed at calcination temperature above 400 °C. The high acid strength and acidity was responsible for the W O bond nature of the complex formed by the interaction between WO 3 and TiO 2. The catalytic activities for ethylene dimerization were correlated with the acidity of the catalysts measured by the ammonia chemisorption method. Catalysts without NiO or WO 3 were inactive as catalysts for ethylene dimerization, because the active sites of ethylene dimerization consist of low valent nickel ion and acidity.

Full Text
Paper version not known

Talk to us

Join us for a 30 min session where you can share your feedback and ask us any queries you have

Schedule a call

Disclaimer: All third-party content on this website/platform is and will remain the property of their respective owners and is provided on "as is" basis without any warranties, express or implied. Use of third-party content does not indicate any affiliation, sponsorship with or endorsement by them. Any references to third-party content is to identify the corresponding services and shall be considered fair use under The CopyrightLaw.