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Valorisation of glycerol by-product of biodiesel production from crude palm oil (CPO) by catalytic conversion
Author(s)
Date Issued
April 11, 2024
Type
Conference Paper
Abstract
Valorisation of glycerol through catalytic conversion conducted using KOH base catalysts with a mass ratio of KOH/glycerol of 0.08 (w/w) was carried out at temperature variations of 230 °C and 300 °C with feedstock variations of pure glycerol (98%) and crude glycerol with a total reaction time of 2 hours. Crude glycerol was obtained from the by-product of biodiesel transesterification from crude palm oil (CPO) using a KOH catalyst of 1% by weight of crude palm oil with variations in CPO:methanol such as 1:3, 1:6, and 2:1, which were performed at 60 °C for 4 hours at stirring speeds of 400 rpm. The largest percentage of crude glycerol conversion was obtained from the variation CPO: methanol (2:1) of 30.67%. The GC-MS characterization of glycerol catalytic conversion products revealed that the highest yield percentage is on the variation of pure glycerol feedstock at 230 °C, with the long-chain hydrocarbon fraction in the form of stearic acid compounds having the highest abundance percentage (abundance percentage of 26.54%). Catalyticconversion of pure glycerol feedstock variations at a reaction temperature of 300 °C resulted in formic acid (abundance percentage of 24.68%) with the greatest abundance and oxalic acid (abundance percentage of 2.28%). Meanwhile, the feedstock variation of crude glycerol produced 2-propenoic acid (abundance percentage of 5.04%) and acetone (abundance percentage of 2.84%), as well as hexadecanoic acid with the largest abundance percentage (32.04%). These findings demonstrated that catalytic glycerol conversion with KOH catalysts produced compounds with a wide range of industrial applications.
Citation
Aip Conference Proceedings, 3071(1), 2024