The glycerolysis of triglycerides (TG) to produce monoglycerides (MG) is an important pathway for glycerol valorization. However, mass transfer resistance has significantly hindered the process efficiency because the reaction is a two-phase liquid-liquid reaction. In this study, a homogenizer was used as a high shear mixing reactor (HSM) to address such issue of mass transfer resistance, and was compared to a conventional mechanically stirred reactor (MS). The effects of the rotational speed, catalyst amount, molar ratio of Gly-to-TG, reaction temperature and reaction time on MG yield were investigated using NaOH as a homogeneous catalyst. Three reaction variables were investigated by statistical analysis using the Box-Behnken (BBK) experimental design, including Gly-to-TG molar ratio (2:1–4:1), catalyst loading (0.1–0.3 wt% TG), and reaction time (15–45 min). The results indicated that the predicted maximum MG yield of 63.4 % was achieved at a reaction time of 29 min, a Gly-to-TG molar ratio of 2.7:1, and a catalyst loading of 0.274 wt% of TG, which agreed with the experimental results. The yield efficiency of HSM was 1.27×10−4 g/J, which was 9.14-fold higher than that of MS at 1.39×10−5 g/J.