Abstract

Calcium oxide was obtained from waste fish bones that has been carried out systematically by decomposition at various temperatures that 800oC, 900oC and 1000oC for 4 hours. Calcium oxide from the decomposition process was characterized using XRD, FTIR, SEM EDX and SAA. The result of XRD Diffractogram showed that the crystallinity increased as the calcination temperature increased. The absorption bands in the FTIR spectra of calcium oxide from calcined waste fish bones shown at 355 cm-1 region indicated CaO vibration, which was reinforced by the emergence of a peak at 859 cm-1. Based on the analysis using SEM EDX, the calcined waste fish bones typically irregular particles and contained dominant calcium element. The low value of BET surface area and the total of pore volume were consistent with the adsorption measurement with SAA. The calcium oxide was applied for biodiesel synthesis from Waste cooking oil through transesterification reaction. The result of the optimization that the calcium oxide was decomposed from waste fish bones at 900oC. It exhibited best catalytic activity in the transesterification of waste cooking oil providing maximum biodiesel yield of 93% at 4% (w/v) of catalyst loading. The decomposition of biodiesel are determined by GC MS that produced methyl palmitate, methyl linoleate, methyl elaidate, methyl linoleolate, methyl stearate and methyl linolenate.

Highlights

  • Biodiesel synthesis from waste cooking oil as an alternative energy source have been reported

  • Calcium oxide (CaO) from fishbone waste was obtained through thermal decomposition at 800oC, 900oCand 1000oC for 4 hours (Farooq & Ramli, 2015)

  • The purpose of XRD analysis is to determine the crystallinity of synthesized calcium oxide catalyst

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Summary

Introduction

Biodiesel synthesis from waste cooking oil as an alternative energy source have been reported. Biodiesel production via transesterfication process used acid/base catalyst as well as enzyme. Catalyst activity in biodiesel production yield conversion of 98%, 99% and 91% for homogeneous base and acid catalyst and enzyme respectively (Mittelbach & Remschmidt, 2004). Homogeneous catalyst is perfectly soluble in glycerol and partially soluble in biodiesel. Separation process is needed to separate the catalyst from product and reactant which might increase operational cost. In order to solve this problem, transesterification process using heterogeneous

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