This study investigates
the synthesis of monoglycerides
(MGs) and
diglycerides (DGs) from glycerol (G) and fatty acid methyl ester (FAME)
using a static mixer reactor (SMR), which combines a static mixer
(SM) with a reactor tank. The SMR integrates Kenics static mixers
(KSM) and low-pressure drop static mixers (LPDSM) with varying length-to-diameter
ratios (L/D = 1.0 and 1.5). Keys glycerolysis parameters, including
the G:FAME molar ratio of 2:1–3:1, 2–3 wt % potassium
hydroxide (KOH), and reaction time of 30–90 min at 150 °C
were systematically explored. The SMR design allows precise control
over the reaction time without altering the feed flow rate or tube
length and avoiding agitator leakage. The optimal operating conditions,
determined through a face-centered central composite design, resulted
in 71.35% MGs and 14.20% DGs at a 3:1 molar ratio of G to FAME, 3
wt % KOH, 60 min, and 150 °C using an LPDSM with an L/D of 1.5.
In comparison, an LPDSM with an L/D of 1 achieved 79.28% MGs and 10.17%
DGs under the same conditions. When applied to purified crude glycerol,
these conditions yielded 61.09% MGs and 23.44% DGs. The study found
that a lower L/D ratio improved the mixing efficiency but increased
the pressure drop. The SMR demonstrated superior performance in glycerolysis
compared with conventional stirred tank reactors and ultrasonic probe
reactors, indicating its potential for enhanced industrial application.