Abstract:
With MCM-41 as support, the supported Ni
2P/MCM-41 catalyst is prepared by first reducing the Ni
2P precursors at low temperature (673 K) and then modifying the surface with air; the as-prepared Ni
2P/MCM-41 catalyst was characterized by X-ray diffraction (XRD), N
2-sorption, scanning electron microscope (SEM), transmission electron microscope (TEM), X-ray photoelectron spectroscopy (XPS) and CO uptake. The catalytic performance of Ni
2P/MCM-41 in hydrodeoxygenation (HDO) of benzofuran (BF) was investigated to elucidate the effect of surface modification with air on the catalyst structure and HDO activity. The results show that pure Ni
2P acts as the active phase on the surface of modified Ni
2P/MCM-41 catalyst; the surface modification can decrease the aggregation of P species and promote the formation of small and highly dispersed Ni
2P active phase. Under 573 K, 3.0 MPa, a weight hourly space velocity of 4.0 h
-1 and a H
2/oil volume ratio of 500, the yield of O-free products reaches 88% for HDO of BF over the modified Ni
2P/MCM-41 catalyst, which is about 50% higher than that over the catalyst prepared by conventional temperature-programmed reduction method.