T90histogram.eps Acta Polytechnica Vol. 52 No. 1/2012 Production of Biodiesel from Vegetable Oil Using Microware Irradiation N. Kapilan Abstract The petroleumoil supply crisis, the increase in demand and the price eruption have led to a search for an alternative fuel of bio-origin in India. Among the alternative fuels, biodiesel is considered as a sustainable renewable alternative fuel to fossil diesel. Non-edible jatropha oil has considerable potential for the production of biodiesel in India. The production of biodiesel from jatropha oil using a conventional heating method takes more than 1h. In this work, microwave irradiation has been used as a source of heat for the transesterification reaction. A domestic microwave oven was modified and used for microwave heating of the reactants. The time taken for biodiesel production using microwave irradiation was 1 min. The fuel property analysis shows that the properties of jatropha oil biodiesel satisfy the biodiesel standards, and are close to the fossil diesel standards. From this work, it is concluded that biodiesel can be produced from vegetable oil using microwave irradiation, with a significant reduction in production time. Keywords: transesterification, jatropha oil, microwave irradiation, biodiesel property. 1 Biodiesel Production 1.1 Introduction The demand for fossil fuel in the world has been in- creasing due to industrialization and the increase in the number of automobiles. According to an esti- mation, world oil resources are judged to be suffi- cient to meet the projected growth in demand until 2030 [1]. The analysis by Shahriar and Erkan [2] in- dicates that the fossil fuel reserves depletion time for crude petroluem oil is approximately 35 year. India is the sixth largest energy consumer, and one of the fastest growing energy consumers in the world, with a rapidly growing economy, a rising population, and an expanding number of middle-class consumers [3]. The government of India is seriously concerned about the fluctuations in global oil prices and consequent expenditure on oil imports. India’s bio-fuel policy now aims to find ways to limit rising oil imports by promoting the use of bio-fuels as a renewable alter- native source for fossil fuels [4]. In recent times there has been greater awareness of biofuels, in particular, biodiesel, and significant attention has been given to the production of biofuels in order to improve the rural economy. Jatropha curcas belongs to the Euphorbiaceae family, and is a small tree or bush with spreading branches. It grows in a number of climatic zones in tropical and sub-tropical regions of the world, and can be grown in areas of low rainfall (250 mm per year minimum, 900–1 200 mm optimal) and in drought- prone areas. It has large green to pale-green leaves, alternate to sub-opposite, three-to-five-lobed with a spiral phyllotaxis, and can attain a height of up to eight or ten meters under favourable conditions. It starts yielding from the second year onwards and con- tinues for 40 years. Generally, fruits are produced in winter when the shrub is leafless. Each inflores- cence yields a bunch of approximately 10 or more ovoid fruits. A three, bi-valved cocci is formed after the seeds mature and the fleshy exocarp dries [5–8]. Figure 1 shows the Jatropha and its seeds. The by- product of oil extraction is seed cake, which contains 24 to 28 % protein on dry basis. The seed cake pro- tein showed most promising results for adhesive and emulsifying properties, which increase the value of the Jatropha. The major fatty acids present in ja- tropha oil are oleic acid, linoleic acid, and palmitic acid. Jatropha is found in tropical America, Africa and Asia [9, 10]. In a combustion study of jatropha oil, it is reported that the fatty acid burned in the first step, and glycerol burned in the second step [11]. a) b) Fig. 1: a) Jatropha, b) Jatropha seeds 46 Acta Polytechnica Vol. 52 No. 1/2012 Masami et al. [12] suggested that a domestic bio- fuel program requires sustained government support, and offer possible justifications for government in- terventions in the production of biofuel. India is a developing country, and imports more than 70 % of its crude oil from other countries, to meet the local energy demand [13]. In India’s bio-fuel policy, Jat- ropha curcas has been identified as the most suitable plant for the biodiesel production. The government of India encourages the planting of Jatropha in waste and degraded lands, with the aim of rural develop- ment and wasteland reclamation [14]. Hence, in this work, jatropha oil was used as the raw material for biodiesel production. Demirbas [15] reported that vegetable oil, biodie- sel, fischer-tropsch and dimethyl ether can be used as a substitute for diesel in diesel engines. How- ever, the direct use of vegetable oil as a substitute for diesel results in higher CO, HC and smoke emis- sions and in lower thermal efficiency of the diesel engine [16]. There are several methods for us- ing vegetable oil as a substitute in diesel engines. One of the most widely used methods is to reduce the viscosity of the vegetable oil by transesterifica- tion [17, 18]. The conventional heating method used in transesterification needs more than one hour reac- tion time to produce a biodiesel yield of more than 90 % [19, 20]. Two-step transesterification is a way of produc- ing biodiesel from crude vegetable oil [21, 22]. Xin et al [23] used an ultrasonic reactor for the production of biodiesel from jatropha oil, using two-step transes- terification. Microwave irradiation has been used for a variety of applications, including organic synthesis. In recent years, microwave irradiation has been used for the production of biodiesel. Yaakob et al. [24] used single-step, base catalyst transesterification for the production of biodiesel from jatropha oil. How- ever, this method required a longer reaction time of 7 min and a higher catalyst concentration of 4 %. In this work, a feasibility study has therefore been car- ried out to produce biodiesel from jatropha oil using two-step transesterification. 1.2 Materials Jatropha oil was collected from the University of Agricultural Sciences, Bangalore, India. This oil was filtered and used for the production of biodiesel. An alkaline catalyst can be used as an excellent mi- crowave irradiation absorber. In this work, sodium hydroxide was used as a catalyst. In comparison with other alcohols, methanol is cheaper and has better physical and chemical properties (polar and shortest chain alcohol), and it was used as a reactant. Sodium hydroxide, methanol and sulphuric acid were pur- chased from Merck Company, India. All the chem- icals used for transesterification were of analytical reagent grade. 1.2.1 Biodiesel production Jatropha oil contains an initial acid value of 9 mgKOH per g of oil, and two-step transesterification was therefore used. In the first step, acid catalyzed transesterfication was used to reduce the acid value from 9 to 1 mgKOH per g of oil based on the con- ditions (0.60 w/w methanol-to-oil ratio and 1 % w/w H2SO4) recommended for the conventional method reported in the literature [22], at a reaction time of 1 min. The experimental setup used in the first step consists of a 250 ml round bottom flask, equipped with a reflux condenser, a mechanical stirrer and a stopper. The scheme is shown in Figure 2. A domes- tic microwave oven was used for microwave irradia- tion. Fig. 2: Microwave-assisted biodiesel production unit Pre-treated jatropha oil was used in base catalyst second-step transesterification. In the second step, transesterification was carried out at a methanol-to- oil ratio of 0.24 w/w and 1.4 % w/w NaOH [22], with a reaction time of 1 min and with power supply 100 W. After the reaction, the excess methanol was removed by vacuum distillation and then the trans- esterification products were poured into a separat- ing funnel for phase separation. After phase sepa- ration, the top layer (biodiesel), was separated and washed with distilled water in order to remove the impurities. Then the biodiesel was heated above 100 ◦C, to remove the moisture. Then the sample was sent for NMR analysis, to find the biodiesel yield. The biodiesel sample was dissolved in chloroform-d (CDCl3) and the proton NMR spectra were obtained using a Bruker AMX 400 spectrometer operating at 300 MHz. Experimental errors can arise from the instru- ments that are used. Uncertainty analysis is therefore needed to prove the accuracy of the experiments. In the present work, uncertainty analysis was performed as per reference [27], and was found to be ±1.5 %. 47 Acta Polytechnica Vol. 52 No. 1/2012 1.3 Determination of fuel properties The flash point of the biodiesel and diesel were de- termined as per the ASTM D 93 method. The pour point determinations were made using the ASTM D 97 method. The kinematic viscosity was determined using a viscometer and according to the ASTM D 7042 method. The density of the fuel was determined using a relative density bottle. The calorific value of the fuel was estimated by a bomb calorimeter. The ash content was determined using an electric muffle furnace, and a copper corrosion test was carried out by the copper strip tarnish test, following the ASTM D 130 method. The water content was determined following the ASTM D 95 method. The acid value of the biodiesel was measured following the ASTM D 974 method. 1.4 Results and discussion Biodiesel was produced from jatropha oil by mi- crowave irradiation, and the biodiesel yield was de- termined using the NMR spectrum. In the NMR spectra, triglycerides (TG) protons on acyl groups resonate at 0.8–2.9 ppm, while protons H-1, H-2 and H-3, appear at a downfield of 4.0–5.6 ppm. When one or two acyl groups migrate from TGs, H-1, H- 2 and H-3 shift toward a higher field. This is due to loss of the high electron density of the acyl group. Figure 3 shows the NMR spectrum of biodiesel. Com- pared to the NMR spectrum of jatropha oil, a large signal at 3.6 pm was observed, which was assigned to the methyl protons of the esters. In addition, some new peaks appeared. This was attributed to the methanolysis products of mono and di-glycerides. The conversion of raw oil to biodiesel was calculated on the basis of the references [26]. A higher biodiesel yield was determined and found to be 0.91 g/g of jatropha oil. Biodiesel production by microwave ir- radiation was due to direct adsorption of the radi- ation by the polar group (OH group) of the reac- tant. It is speculated that the OH group is directly excited by microwave radiation, and the local tem- perature around the OH group would be very much higher than its environment. Hence, microwave as- sisted transesterification is a way of reducing the re- action time, the electrical energy and labour costs as compared to the conventional method. The power consumption in this method was 16.6 J/kg of jat- ropha oil. Fig. 3: NMR spectra of biodiesel Table 1 compares the properties of jatropha biodiesel with the properties of diesel. The flash point of biodiesel satisfies the fuel standards and is better than the flashpoint diesel. This is an impor- tant safety consideration when handling and storing flammable materials. The important cold flow prop- erties of biodiesel are the cloud and pour point. Ac- cording to ASTM standard D 6751, no limit is given for pour point and suggested “report” in the fuel standard. The calorific value is an important prop- erty of biodiesel that determines its suitability as an alternative to diesel. In the ASTM and BIS standard, no limit is given for the calorific value. However, in the European standard, EN 14214, the approved calorific value for biodiesel is 35 MJ per kg. The ta- ble shows that the calorific value of MOB is close to that of diesel. Table 1: Fuel properties Property ASTM D6751 Biodiesel Diesel Flash point (◦C) > 130 132 68 Pour point (◦C) – 6 −15 Calorific Value (MJ/kg) – 37.95 42.71 Viscosity at 40◦C (mm2/sec) 1.9–6 4.21 2.28 Density at 15◦C (kg/m3) – 889 846 Water content (mg/kg) < 500 129 102 Acid number (mg KOH/g) < 0.50 0.42 0.34 Copper strip corrosion >No. 3 1 1 Ash Content (%) < 0.02 0.01 0.01 48 Acta Polytechnica Vol. 52 No. 1/2012 According to the ASTM standards, the ac- ceptable viscosity range for biodiesel is between 1.9–6.0 mm2/s at 40 ◦C, and MOB satisfies the biodiesel standard. The density of MOB is close to that of diesel and satisfies the BIS standard. The ASTM and BIS biodiesel standard approves a maxi- mum acid value for biodiesel of 0.5 mg KOH/g, and this was fulfilled by MOB. The degree of tarnish on the corroded copper strip correlates to the overall corrosiveness of the fuel sample. The copper strip corrosion property of MOB is within the specifica- tions of ASTM and BIS. Another important factor of biodiesel is the ash content estimation. The ash content of MOB satisfies both the ASTM standard and the BIS standard. 2 Conclusions In this work, biodiesel was produced from jatropha oil using microwave irradiation and with the help of two-step transesterfication. It was observed that microwave irradiation helps the synthesis of methyl esters (biodiesel) from non-edible oil, and higher biodiesel conversion can be obtained within a few minutes, whereas the conventional heating process takes more than 60 minutes. Biodiesel produced by microwave irradiation satisfies the ASTM and BIS biodiesel standards. Acknowledgement The author wishes to thank Visvesvaraya Techno- logical University, Belgaum, for financially support- ing this work (Grant No. VTU/Aca./2009-10/A- 9/11583, 2009). References [1] Chedid, R., Kobrosly, M., Ghajar, R.: A supply model for crude oil and natural gas in the Middle East, Energy policy, 35, 2007, 2 096–2 109. 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