The aim of this work was to study the efficiency of biofuel production from bio-oils (Palm oil
(PO) and Waste cooking oil (WCO)) in pack-bed reactor with reaction temperature at 450, 500, 550°C
under atmospheric pressure and WHSV of 0.5 h-1. The dolomite as a catalyst were pressed to cylindrical
pellets and then calcined at 600°C for 4 hr. The physical and chemical properties of catalysts were
characterized by X-ray fluorescence spectroscopy (XRF), X-ray diffraction (XRD), N2 adsorptiondesorption
and Field emission scanning electron microscope (FE-SEM). The results found that the main
compositions of catalyst were CaO, SiO2 and Fe2O3. In addition, the crystalline structures of catalyst
before calcination appeared Ca(OH)2, CaCO3, CaO and SiO2. However, after calcination the crystalline
structures showed Ca(OH)2, CaO, SiO2. The specific surface area decreased because of the phase
transformation and thermal decomposition to oxide form of catalyst. The surface morphology of
dolomite before calcination showed large particle sizes and smooth surface. The morphology was
different after calcination, which obvious in small particle sizes and roughness surface. The highest
pyrolytic oil products of PO and WCO were about 90%. Additionally, the products of PO reacted at
450°C gave the highest products, whereas the products of WCO reacted at 550°C showed the highest
product yield. The liquid products were distilled following ASTM D86 to separate gasoline and diesel
oils. Then, the properties of distilled products were analyzed for viscosity and heating value following
ASTM D445 and ASTM D240, respectively. The heating value and viscosity of distilled products
followed the standard values. Therefore, this process can produce the bio-fuel oils.