Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst

A kinetic study of free fatty esterification was carried out using Purolite D5081 as a catalyst. Esterification reaction was carried out using 1.25% (w/w) catalyst loading, 6:1 methanol to oil feed mole ratio, 350 rpm stirring speed and reaction temperatures ranging from 323 - 335 K. The experimenta...

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Bibliographic Details
Main Authors: Sumaiya, Zainal Abidin, Vladisavljević, Goran T., Saha, Basudeb
Format: Conference or Workshop Item
Language:English
Published: 2014
Subjects:
Online Access:http://umpir.ump.edu.my/id/eprint/8516/
http://umpir.ump.edu.my/id/eprint/8516/1/Kinetics_of_Free_Fatty_Acid_Esterification_in_Used_Cooking_Oil_Using_Ion_Exchange_Resin_as_Catalyst.pdf
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Summary:A kinetic study of free fatty esterification was carried out using Purolite D5081 as a catalyst. Esterification reaction was carried out using 1.25% (w/w) catalyst loading, 6:1 methanol to oil feed mole ratio, 350 rpm stirring speed and reaction temperatures ranging from 323 - 335 K. The experimental data from the esterification reaction were fitted to three kinetic models: Pseudo Homogeneous (PH), Eley-Rideal (ER) and Langmuir-Hinshelwood-Hougen-Watson (LHHW)models. A built-in ODE45 solver in MATLAB 7.0 was used to numerically integrate the differential molar balances describing the concentration of FFA in the system.