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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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/8516/3/Kinetics_of_Free_Fatty_Acid_Esterification_in_Used_Cooking_Oil_Using_Ion_Exchange_Resin_as_Catalyst.pdf
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author Sumaiya, Zainal Abidin
Vladisavljević, Goran T.
Saha, Basudeb
author_facet Sumaiya, Zainal Abidin
Vladisavljević, Goran T.
Saha, Basudeb
author_sort Sumaiya, Zainal Abidin
collection UMP
description 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.
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spelling UMPir85162022-11-03T01:22:55Z http://umpir.ump.edu.my/id/eprint/8516/ Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst Sumaiya, Zainal Abidin Vladisavljević, Goran T. Saha, Basudeb TP Chemical technology 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. 2014 Conference or Workshop Item PeerReviewed pdf en http://umpir.ump.edu.my/id/eprint/8516/3/Kinetics_of_Free_Fatty_Acid_Esterification_in_Used_Cooking_Oil_Using_Ion_Exchange_Resin_as_Catalyst.pdf Sumaiya, Zainal Abidin and Vladisavljević, Goran T. and Saha, Basudeb (2014) Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst. In: International Conference on Chemical, Biological and Environmental Engineering (ICBEE 2014) , 15-16 Sepember 2014 , Paris, France. pp. 24-28.. (In Press / Online First) (In Press / Online First)
spellingShingle TP Chemical technology
Sumaiya, Zainal Abidin
Vladisavljević, Goran T.
Saha, Basudeb
Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title_full Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title_fullStr Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title_full_unstemmed Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title_short Kinetics of Free Fatty Acid Esterification in Used Cooking Oil Using Ion Exchange Resin as Catalyst
title_sort kinetics of free fatty acid esterification in used cooking oil using ion exchange resin as catalyst
topic TP Chemical technology
url http://umpir.ump.edu.my/id/eprint/8516/3/Kinetics_of_Free_Fatty_Acid_Esterification_in_Used_Cooking_Oil_Using_Ion_Exchange_Resin_as_Catalyst.pdf
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