Waste cooking oil (WCO) is dispersed in tetralin or dodecane and hydrotreated in a batch reactor over a fabricated NiMo/gamma-Al2O3-beta-zeolite catalyst. The properties of catalysts are controlled by adjusting the mass fraction of beta-zeolite in support (x), the mass fraction of NiO and MoO3 (m) and Ni/(Ni + Mo) mol fraction (y) in catalysts. The effects of the catalytic properties, solvents and reaction conditions on the hydrodeoxygenation of WCO are investigated. The results showed that increasing m and y promoted WCO conversion and the formation of alkane hydrocarbons; the addition of Ni into Mo helped to promote the reducing ability of catalysts and enhanced deoxygenation via decarboxylation/decarbonylation pathway. An increase in beta-zeolite was unfavourable for WCO conversion. A complete conversion of WCO to hydrocarbons was achieved at 350 degrees C under H-2 at 5 MPa for 3 h with dodecane as solvent. The isomerized compounds accounted for less than 10 wt%. A low H-2 pressure is suitable for tetralin exerting hydrogen-donating effect. (C) 2018 Elsevier Ltd. All rights reserved.