Abstract:Reaction conditions for the NiMo/Al2O3-catalyzed production of bio-paraffins through an integrated process combining hydrodeoxygenation (HDO) of fatty acid methyl esters (FAMEs) derived from waste cooking oils and the subsequent hydrodenitrogenation (HDN) have been optimized in the following work. Under the optimal HDO conditions containing a temperature of 380 ℃, a hydrogen pressure of 2 MPa, a H2/FAMEs volume ratio of 1000, and a space velocity of 1 h-1, the presulfided NiMo/Al2O3 catalysts converted FAMEs to bio-paraffins with an overall selectivity of normal alkanes above 97%. The employed catalysts showed enough structural stability and high resistance to coke in the HDO of FAMEs, with an identical structure to the fresh catalysts observed and an amount of deposited carbonaceous species at 3.18% measured after reaction for 1000 h. However, the deoxygenated products appeared to be colored, especially after an exposure to sunlight, due to the undecomposed residual fragments of chlorophyll. The following HDN reaction over NiMo/Al2O3 catalysts reduced significantly their fluorescence and removed more than 90% nitrogen-containing impurities in the bio-paraffins under conditions of a temperature of 310 ℃, a hydrogen pressure of 2 MPa, a H2/paraffin volume ratio of 2000, and a space velocity of 0.25 h-1.