Chinese Journal of Catalysis ›› 2012, Vol. 33 ›› Issue (9): 1586-1593.DOI: 10.3724/SP.J.1088.2012.20330

• Research papers • Previous Articles     Next Articles

Hydrothermal Synthesis of TiO2-Al2O3 Composite Oxide and Catalytic Performance of Its Suppored NiMoP for Hydrodesulfurization of FCC Diesel

HONG Wei1,3, LIU Baijun1,a, WANG Hongbin2, CHEN Yu1,b   

  1. 1State Key Laboratory of Heavy Oil Processing, the Key Laboratory of Catalysis of CNPC, Faculty of Chemical Engineering, China University of Petroleum, Beijing 102249, China; 2Shenyang Sanjukaite Catalyst Co., Ltd., Shenyang 110144, Liaoning, China; 3China Petroleum Engineering &Construction Corporation Beijing Engineering Branch, Beijing 100101, China
  • Received:2012-04-19 Revised:2012-06-21 Online:2012-09-11 Published:2012-09-11

Abstract:  The TiO2-Al2O3 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 TiO2-Al2O3 composite oxide were studied. The composite oxide and NiMoP/TiO2-Al2O3 catalyst were characterized by powder X-ray diffraction, N2 adsorption-desorption, scanning electron microscopy (SEM), thermogravimetric and differential thermal analysis (TG-DTA), NH3 temperature-programmed desorption (NH3-TPD), pyridine adsorption in situ infrared spectroscopy (Py-FTIR), and H2 temperature-programmed reduction (H2-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 TiO2-Al2O3 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 TiO2-Al2O3 composite oxide could reach up to 266 m2/g and 0.58 cm3/g, respectively. The specific surface area of NiMoP/TiO2-Al2O3 catalyst also reached as high as 175 m2/g. The results of NH3-TPD and Py-FTIR show that NiMoP/TiO2-Al2O3 catalyst has a weak acidity wherein Lewis acid is dominative. The NiMoP/TiO2-Al2O3 catalyst has higher desulfurization activity due to the existence of TiO2, which can decrease the strong interaction between the active phase and the support. Hydrodesulfurization activity for FCC diesel over NiMoP/TiO2-Al2O3 catalyst is thus 5.4% higher than that on the NiMoP/Al2O3 catalyst.

Key words: titania, alumina, composite oxide, hydrothermal synthesis, polyethylene glycol, fluid catalytic cracking diesel, hydrodesulfurization