In this work zeolites HY, HZSM-5 and mixes of zeolites with gama - Al2O3 in different ratios were taken as carriers for 0.8 wt percent Pd catalysts. Physico-chemical characteristics of the catalysts were determined by methods of Brunauer-Emmett-Teller (BET)-N2 adsorption, x-ray diffraction (XRD), scanning electron microscopy (SEM), energy dispersive x-ray spectroscopy (EDS), transmission electron microscopy (TEM), temperature-programmed reduction (TPR), hydrogen pulse chemisorption (HPC) and NH3 adsorption-desorption. The activity of catalysts was studied at 225-450°C, at 0.1 and 0.7 MPa with molar ratio of H2:n-C6H14 = 5.92 and n-hexane concentration 9.2 mol percent. Mixing of gama-Al2O3 with zeolite made acidity of catalyst weaken and led to a decrease of Pd cluster size, to an increase of Pd dispersity and a reduction of the extent of Pd in the case of catalyst Pd/HY
but for the catalyst Pd/HZSM-5 such mixing led to the reverse effect. That is why the increase of activity in the first case and the decrease of activity in the second case have been observed. It has been found that the optimal ratio of mixed carrier is gama-Al2O3: HY = 2.5: I and the optimal calcined temperature of NH4ZSM-5 to obtain HZSM-5 is 500-550°C. An increase of reaction pressure from 0.1 to 0.7 MPa remarkably increased the activity, selectivity and stability of Pd-based catalysts.