Abstract

In this study, continuous transesterification of refined palm oil by using radiation-induced kenaf denoted as anion exchange kenaf catalyst in a packed-bed reactor was developed. The application of full factorial design and response surface methodology (RSM) based on the central composite design (CCD) was used to design the process and analyzed the effect of reactor operating variables such as packed bed height, the molar ratio of oil to ethanol and volumetric flow rate on the production of fatty acid ethyl ester (FAEE). The statistical analysis results showed that all three operating parameters affect the reaction efficiency significantly. The optimum conditions were determined to be 9.81 cm packed bed height, a molar ratio at 1:50, and a volumetric flow rate of 0.38 mL min−1. Three tests were carried out to verify the optimum combination of process parameters. The predicted and actual values of molar conversion fatty acid ethyl ester (FAEE) molar conversion were 97.29% and 96.87%, respectively. The reusability of kenaf fiber-based catalysts is discussed with a specially highlighted on fiber dissolution, leaching, and fouling. Nevertheless, the impurities absorption properties of anion exchange kenaf catalyst towards biodiesel production could eventually simplify the biodiesel purification steps and cost. In sum, anion exchange kenaf catalyst shows the potential commercial applications to transesterification of FAEE in a packed-bed reactor.

Highlights

  • The consciousness of environmental problems and energy issues related to fossil fuels has encouraged many researchers to explore the possibility of using renewable fuels instead of fossil fuels

  • This conventional catalyst achieves great conversion yields; it is not suitable to be used to produce biodiesel from high free fatty acid feedstocks as it is highly sensitive to the presence of water and free fatty acid (FFA) which leads to soap formation and hindered the conversion of biodiesel

  • This study aims to utilize a bio-based heterogeneous catalyst derived from kenaf fiber fabricated by radiation-induced graft polymerization for transesterification of refined palm oil into biodiesel in a packed-bed reactor

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Summary

Introduction

The consciousness of environmental problems and energy issues related to fossil fuels has encouraged many researchers to explore the possibility of using renewable fuels instead of fossil fuels. The batch homogenous catalytic is a simple, cheap and short time, the major drawbacks associated with the process are that the homogeneous catalyst is corrosive, difficult to reuse, and unnecessarily complex separation of by-product [5]. This conventional catalyst achieves great conversion yields; it is not suitable to be used to produce biodiesel from high free fatty acid feedstocks as it is highly sensitive to the presence of water and free fatty acid (FFA) which leads to soap formation and hindered the conversion of biodiesel. The additional complicated and costly purification processes for homogenous catalyzed batch transesterification can cause an undesirable effect on the economic and environmental [6]

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