The TiO
2-Al
2O
3 composite oxide was synthesized by the hydrothermal method. The effects of hydrothermal temperature, reactant concentration, average molecular mass of polyethylene glycol, and polyethylene glycol concentration on the structural and textural properties of TiO
2-Al
2O
3 composite oxide were studied. The composite oxide and NiMoP/TiO
2-Al
2O
3 catalyst were characterized by powder X-ray diffraction, N
2 adsorption-desorption, scanning electron microscopy (SEM),
thermogravimetric and differential thermal analysis (TG-DTA), NH
3 temperature-programmed desorption (NH
3-TPD), pyridine adsorption in situ infrared spectroscopy (Py-FTIR), and H
2 temperature-programmed reduction (H
2-TPR). The catalytic performance of the catalyst for hydrodesulfurization of
fluid catalytic cracking (FCC) diesel was evaluated in a fixed-bed reactor with medium pressure. The results show that both specific surface area and pore volume of the TiO
2-Al
2O
3 composite oxide increased with increasing hydrothermal temperature, reactant concentration, average molecular mass of polyethylene glycol, and polyethylene glycol concentration. Under the optimum conditions, the specific surface area and pore volume of the TiO
2-Al
2O
3 composite oxide could reach up to 266 m
2/g and 0.58 cm
3/g, respectively. The specific surface area of NiMoP/TiO
2-Al
2O
3 catalyst also reached as high as 175 m
2/g. The results of NH
3-TPD and Py-FTIR show that NiMoP/TiO
2-Al
2O
3 catalyst has a weak acidity wherein Lewis acid is dominative. The NiMoP/TiO
2-Al
2O
3 catalyst has higher desulfurization activity due to the existence of TiO
2, which can decrease the strong interaction between the active phase and the support. Hydrodesulfurization activity for FCC diesel over NiMoP/TiO
2-Al
2O
3 catalyst is thus 5.4% higher than that on the NiMoP/Al
2O
3 catalyst.