This study presents manufacturing jet fuel-range (C9-C15) hydrocarbon biofuels from 2-methylfuran and furfural. The process involves a hydroxyalkylation-alkylation reaction, followed by hydrodeoxygenation of the C15 fuel precursor. The hydroxyalkylation-alkylation reaction was investigated under various cation exchange resin loadings, furfural/2-methylfuran molar ratios, and reaction temperatures. The hydroxyalkylation-alkylation reaction results were further corroborated by an appropriate kinetic model. Hydrodeoxygenation proceeds via the sequential furan ring-hydrogenation and ring-opening reactions, followed by the combination of dehydroformylation, hydrodeoxygenation, and cracking reactions. The dehydroformylation reaction was the leading pathway over a Ni/γ-Al2O3 catalyst, forming mainly C14H30 alkane. The oxygenate conversion was boosted with rising hydrogen pressure, Ni metal content on γ-Al2O3, and reaction temperatures. Both hydrodeoxygenation and hydrogenation reactions proliferated at elevated hydrogen pressure with the enrichment of the C15 alkane and ring-opening and ringhydrogenation products. The cracking, ring-opening, and ring-hydrogenation reactions were promoted at elevated reaction temperatures with a significant amount of lighter alkanes. © 2022 The Author(s).