Owing to the decrease of global oil price, development of downstream value-added products is important to biodiesel industry. In this study, we used palmitic acid methyl ester (PAME) as a starting material to produce 2-ethylhexyl palmitate (2-EHP), an environmentally friendly biolubricant product, which was derived from the transesterification of fatty acid methyl esters and long chain fatty alcohols. Conventional synthetic routes of 2-EHP have disadvantages, including high catalyst price, low conversion efficiency, and pollution issues. To solve these problems, in situ transesterification of PAME with 2-ethylhexanol (2-EH) was conducted over unsupported potassium carbonate as heterogeneous catalyst. The optimal reaction temperature, 2-EH to PAME molar ratio, and catalyst to PAME mass ratio were 180 C, 3:1, and 3.0 wt%, respectively. The PAME conversion reached up to 100% within 1 hour under the optimal conditions. In addition, a kinetic model describing the experimental data over a temperature range of 160-180 C was developed. The dependence of kinetic rate constant (k) on temperature was evaluated, and the activation energy (E a ) for the transesterification of PAME with 2-EH was calculated to be 57.04 kJ mol Nomenclature PAME palmitic acid methyl ester 2-EHP 2-ethylhexyl palmitate 2-EH 2-ethylhexanol WCO waste cooking oil DMC double-metal cyanide complex catalyst GC gas chromatography IC ion chromatography A 2-EHP the peak area of 2-EHP A PAME the peak area of PAME f 2-EHP the response factor of 2-EHP to PAME X i the concentration of potassium ions in sample c i the concentration of potassium ions in the measured solution c 0 the concentration of potassium ions in the blank solution V the dilution coefficient m the mass of the sample X PAME degree of PAME conversion t time (min) m cat the mass ratio of catalyst (g) cat catalyst T reac reaction temperature ( C) reac reaction r PAME reaction rate (mol L