ARTICLE IN PRESS

SULPHONIC ACIDS SUPPORTED ON Fe3O4/PVA MAGNETIC COMPOSITE AS CATALYSTS FOR ESTERIFICATION OF FREE FATTY ACIDS

ANDREW T. H. YEOW1,2; ADEEB HAYYAN1,2*; MOHD USMAN MOHD JUNAIDI1,2; MUNEER M. BA-ABBAD3 and MOHD ALI HASHIM1

DOI: https://doi.org/10.21894/jopr.2024.0042
Received: 11 January 2024   Accepted: 13 June 2024   Published Online: 4 September 2024
ABSTRACT

Low-quality palm oil (LPO) with high free fatty acid (FFA) content (9.66%) can be pretreated for biodiesel production through acid-catalysed esterification. However, homogeneous acid catalysts exhibit challenges in recyclability and separation despite their high catalytic efficiency. Magnetic composites (Fe3O4/PVA) as support materials for acid catalysts are a viable protocol for improving recyclability and separation performances. In this study, sulphonic acids and their deep eutectic solvent (DES) counterparts (formed with paracetamol at a 3:1 molar ratio) were supported on Fe3O4/PVA to yield heterogeneous solid acid catalysts for FFA esterification in LPO. From the screening results, Fe3O4/PVA/PTSA was determined as the best performing catalyst. The optimised reaction conditions were determined: 10 wt.% catalyst loading, 20:1 methanol-to-oil molar ratio, 5 hr of contact time and at 60°C, resulting in an FFA conversion of 79.81%. Fe3O4/PVA/PTSA exhibited fair recyclability performances and stability with > 65% FFA conversion after five successive runs. FFA esterification reaction using Fe3O4/PVA/PTSA was determined to require an activation energy of 43.72 kJ/mol following a simplified pseudo first order rate of reaction. Pristine sulphonic acids exhibited higher compatibility to be supported on Fe3O4/PVA magnetic composite than their DES counterpart, with Fe3O4/PVA/PTSA being a viable catalyst for the pretreatment of low-quality oils through FFA esterification.

KEYWORDS:


1 Department of Chemical Engineering,
Faculty of Engineering, Universiti Malaya,
50603 Kuala Lumpur, Malaysia.

2 Sustainable Process Engineering Centre (SPEC),
Faculty of Engineering, Universiti Malaya,
50603 Kuala Lumpur, Malaysia.

3 Gas Processing Center,
College of Engineering, Qatar University,
P.O. Box 2713 Doha, Qatar.

* Corresponding author e-mail: adeeb.hayyan@yahoo.com