Esterification reaction of free fatty acid in used cooking oil using sulfonated hypercrosslinked exchange resin as catalyst

Nurul Asmawati, Roslan and Sumaiya, Zainal Abidin and Norhayati, Abdullah and Osazuwa, Osarieme Uyi and Ruwaida, Abdul Rasid and Nursofia, Mohd Yunus (2021) Esterification reaction of free fatty acid in used cooking oil using sulfonated hypercrosslinked exchange resin as catalyst. Chemical Engineering Research and Design, 180. pp. 414-424. ISSN 0263-8762. (Published)

Pdf Esterification reaction of free fatty acid.pdf Restricted to Repository staff only Download (3MB) | Request a copy

Abstract

The production of valuable fatty acid alkyl ester (FAAE) commercially known as biodiesel from used cooking oil (UCO) as feedstock has recently gained global interest. To carry out this production process, an esterification reaction is necessary to minimize the amount of free fatty acid (FFA) in the UCO. The purpose of this research work is to evaluate the performance of the newly snythesized sulfonated hypercrosslinked exchange resin (SHER) for the esterification reaction. The catalyst was first synthesized and characterized using various physicochemical analyses (i.e. Fourier transform infra-red (FTIR), surface morphology, N2 physisorption analysis and thermogravimetric analysis (TGA)) and further subjected to the esterification reaction to determine the reaction kinetics. The esterification reaction was conducted at various catalyst loading (1−8 wt%), reaction temperatures (40−60 ◦C), and methanol to oil molar ratios (6:1−24:1). From the characterization study, SHER was found to have high decomposition temperature (up to 398 ◦C) and specific surface area (836 m2 g−1). Additionally, SHER had the capability to accommodate high number of active sites which could benefit the esterification reaction. The highest FFA conversion of 97% was achieved at 5 wt% catalyst loading, 60 ◦C of reaction temperature and 12:1 methanol to oil mole ratio in 2 h reaction time. Analyses of the spent catalyst revealed the presence of impurities residue on the SHER’s surface following the esterification reaction, and the catalyst pore remained evident even after several reusability cycles. Finally, the Eley-Rideal, pseudo-homogeneous and Langmuir-Hinshelwood-Hougen-Watson kinetic models were proposed. Due to its high activation energy; i.e. 48.4 kJ mol−1, the reaction was found to be limited by surface reaction and governed by the chemical step.

Item Type:	Article
Uncontrolled Keywords:	Used cooking oil, Biodiesel, Esterification, Free fatty acid, Hypercrosslinked exchange resins catalyst, Kinetic
Subjects:	T Technology > TP Chemical technology
Faculty/Division:	Centre of Excellence: Centre of Excellence for Advanced Research in Fluid Flow College of Engineering Faculty of Chemical and Process Engineering Technology
Depositing User:	Prof. Md. Sumaiya Zainal Abidin@ Murad
Date Deposited:	09 May 2022 02:43
Last Modified:	07 Nov 2022 06:44
URI:	http://umpir.ump.edu.my/id/eprint/33967
Download Statistic:	View Download Statistics

Actions (login required)

View Item