International Conference on Global Trends in Engineering, Technology and Management (ICGTETM-2016) Experimental Study: Effect of Process Parameters on Palm Oil Methylester Yield Ajaygiri K. Goswami1, Ghyas. A. Usmani2, Prachi A. Kate3 1 Associate Professor, Department of Chemical Engineering, University Institute of Chemical Technology, North Maharashtra University, Jalgaon – 425001, India 2 Professor, Department of Oil Technology, University Institute of Chemical Technology, North Maharashtra University, Jalgaon – 425001, India 3 Student, Department of Chemical Engineering, University Institute of Chemical Technology, North Maharashtra University, Jalgaon – 425001, India Abstract: The palm oil is the cheapest edible oil. Most poor people consume the palm oil. The cost of palm oil and soybean oil are quite close in Indian market. The biodiesel made by palm oil is good source of an alternative fuel. The cost of manufacturing is also comparatively less and useful byproduct like glycerol is obtained. The experimental study is totally focused on the percentage of palm oil methylester formation on the basis of process parameters, concentration of NaOH catalyst, oil methanol ratio and reaction temperature. This is base catalyzed transesterification reaction. Any two parameters were kept constant and other one parameter was changed, resulting to change in palm oil methyl-ester content. From the experimental studies, the amount of NaOH catalyst required was calculated for which maximum ester yield was obtained. Similarly, methanol palm oil ratio and temperature of transesterification reaction were estimated experimentally to obtain maximum palm oil methylester (Biodiesel) which is useful alternative fuel for petroleum diesel. Keywords: Biodiesel, Transesterification. I. Methylester, Palm Oil, Introduction: The pursuit of alternative fuels has been in the forefront, of which biodiesel is currently considered to be a feasible alternative diesel fuel, as it is being prepared from natural resources which are environmentally benign [1] The biodiesel is made from vegetable oils, animal fats has potential to decrease the demand of petroleum diesel and also having the qualities to decrease the air pollution generated by diesel engine emissions [1,2]. Recently the fuel cost and environmental problems have rapidly increased due to high requirements of diesel vehicles. In country like India, Biodiesel is highly viable as an alternative fuel because the cost of diesel increasing day by day. Fuel production from biological sources has a focused attention to academic as well as industrial experts [3, 4]. In the entire world, the palm oil is mostly consumed alongside a fact that palm oil ISSN: 2231-5381 is the world’s cheapest vegetable oil [2]. As compared to other vegetable oils, the palm oil contains more monosaturated fatty acids. The biodiesel produced from palm oil can be correctly termed as Fatty Acid Methyl Ester (FAME) which has the potential to substitute petroleum derived diesel oil. The palm oil is rich source of antioxidants and vitamin E and contains mono, di- and triglycerides [5]. For Biodiesel preparation various stocks available like soybean oil, sunflower oil, neem oil, cottonseed, jatropha, rapeseed oil, canola and palm oil. As comparison with other feedstock, the palm oil has better advantages and potential for biodiesel production. The production of palm oil is continuous [6]. Use of Fatty Acid Methyl Ester as an alternative fuel does have an advantage of low sulphur content, lower aromatic content, higher heat content, biodegradability and liquid nature probability [3] The petroleum properties like density, kinematic viscosity, cetane number, flash point, cloud point are very important. The biodiesel produced from palm oil at 60°C, 60 minutes and at 6:1 methoxide oil ratio and the above mentioned properties of were within the American Standard ASTM D 6751 and European Standard EN 14214 [7]. This represents the palm oil methyl ester run successfully without diesel engine modification. In the present study main focus on production of biodiesel from palm oil in which how the recovery of methylester can be increased by changing the process parameters. From the experiments of several batches the optimum process conditions of transesterification of palm oil was studied. II. Method: The transesterification of palm oil was done for preparation of methylester which is the palm oil biodiesel. The experiments have been carried out in fifteen batches. In the first five batches, the oil methanol ratio was taken 1:6 and the reaction temperature was 65°C. Both oil methanol ratio and temperature taken to be constant for all the five http://www.ijettjournal.org Page 382 International Conference on Global Trends in Engineering, Technology and Management (ICGTETM-2016) batches and the catalyst used i.e. base catalyst NaOH has been increased from 0.2 to 1gm. For next five batches, the oil methanol ratio was taken 1:6 and the catalyst concentration was taken 0.4gm. Both oil methanol ratio and catalyst concentration taken to be constant for all the five batches and the reaction temperature has been increased from 60 to 80°C. For last five batches, the reaction temperature was taken 65°C and the catalyst concentration was taken 0.4gm. Both reaction temperature and catalyst concentration taken to be constant for all the five batches and the oil methanol ratio has been increased from 1:6 to 1:10. The experimental set up containing three neck bottom flask of capacity 500 mL contains a magnetic needle and solution mixture. This is then placed on the magnetic stirrer. The flask has three opening from which central opening is for reflux condenser. The methanol is volatile and vaporized during the reaction so reflux condenser is used to taper so as to return the vapors back into flask. The second opening is for thermometer to monitor the temperature continuously during the reaction and third is for filling the reactants into the flask. Palm oil in a three neck round bottom flask was taken, heated the oil at 110˚C temperature for removing moisture content, cooled & thereafter filtration was done. In the separate beaker, the catalyst NaOH was mixed with the methanol and sodium methoxide was formed. The oil was poured, heating and stirring started at same time. It was heated upto 40˚C & sodium methoxide was added into the round bottom flask by opening, mixing continued for 2-3 hours at specified temperature. The mixture was allowed to settle for 24 hours at which two separate layers were obtained. The top layer was methyl ester of oil and the bottom one of glycerol. Using a conical separating funnel, the glycerol is separated at the bottom. In a good completion reaction glycerol begins to separate immediately when stirring and heating is stopped, two layer i.e. ester and glycerol is separated by means of separating funnel. In the ester, the traces of glycerol, unreacted methanol are present. Soap present in these traces could be removed by adding warm water to the ester and separation was obtained after around three hours. The methanol & soap is separated and glycerol is separated as byproduct. The recovery of methylester is obtained. changes, which results into variations in the biodiesel yield was studied in fifteen batches. A. Oil: Methanol Ratio and Temperature is constant and catalyst concentration changes: Fresh Palm oil was used to prepare biodiesel by transesterification process. First five batches in which Oil: Methanol Ratio and temperature is constant and catalyst concentration changes and recovery of biodiesel is obtained for all five batches. For fresh palm oil, the results of all five batches where oil methanol ratio was 1:6 and temperature 650C was kept constant and concentration of catalyst NaOH changed from 0.2 to 1.0 gm. The graph for the same is as given as follows. Table 1 Percentage Recovery of Biodiesel for Different Concentration of Catalysts Batches 1 2 3 4 5 gm. of NaOH (Concentration of catalyst) gm. of Biodiesel 0.2 0.4 0.6 0.8 1.0 165.5 198.3 176.1 160.5 156.7 % Recovery of Biodiesel 64.47 77.11 68.48 62.41 60.71 III. Results and Discussion: All the three parameters of transesterification process such as reaction temperature, catalyst concentration and oil methanol ratio has optimum value for getting good biodiesel yield. Here two parameters are kept constant and third one is changed and variation in biodiesel yield has been estimated experimentally. Three observation tables where Oil: Methanol Ratio and temperature is constant and catalyst concentration changes, Oil: Methanol Ratio and Concentration are constant and temperature changes, concentration and temperature is constant and Oil: Methanol Ratio ISSN: 2231-5381 Fig. 1 Graph of Catalyst Concentration versus Percentage Recovery of Biodiesel B. Oil: Methanol Ratio and Concentration is kept constant and temperature changes: Fresh Palm oil was used to prepare biodiesel by transesterification process. First five batches in which http://www.ijettjournal.org Page 383 International Conference on Global Trends in Engineering, Technology and Management (ICGTETM-2016) Oil: Methanol Ratio and Concentration is kept constant and temperature changes and recovery of biodiesel was obtained for all five batches. Table 3 Percentage Recovery of Biodiesel for Different Oil: Methanol Ratio Oil methanol ratio i.e. 1:6 and concentration of catalyst i.e. 0.4 gm is kept constant and the temperature is changed from 60 0C to 800C. The graph for the same is given as follows. Batches Oil:Methanol Ratio gm of Biodiesel % recovery of Biodiesel 1 1:6 198.3 77.11 Table 2 Percentage Recovery of Biodiesel for Different temperatures 2 1:7 179.7 68.38 3 1:8 175.5 65.81 4 1:9 167.0 61.85 5 1:10 164.2 60.21 Batches Temp. °C gm of Biodiesel 1 60 185.3 72.06 2 65 198.3 77.11 3 70 176.2 68.52 4 75 164.8 64.08 5 80 153.5 59.69 % recovery of Biodiesel Fig. 3 Graph of Oil: Methanol Ratio versus Percentage Recovery of Biodiesel IV. Conclusion: Fig. 2 Graph of temperature versus Percentage Recovery of Biodiesel C. Concentration & Temperature is constant and Methanol: Oil Ratio changes: Fresh Palm oil was used to prepare biodiesel by transesterification process. First five batches in which concentration and temperature id constant and Oil:Methanol Ratio changes and recovery of biodiesel was obtained for all five batches. Concentration of catalyst being 0.4gm and temperature being 650C are kept constant and oil methanol ratio is changed from 1:6 to 1:10. ISSN: 2231-5381 From the experimental outcomes it has been observed that by taking two parameters constant and changing the remaining, the biodiesel yield either increases or decreases. The optimum values were obtained from the experimental study of fifteen batches for all the three cases in which initially the NaOH concentration is increased and then temperature is increased and finally the methanol oil ratio is increased. The results were obtained from all fifteen batches suggested that for preparing biodiesel from palm oil need the proper values of the process parameters for biodiesel production for the proper conversion of palm oil to methylester (Biodiesel) which can be used as alternative diesel fuel. From the experimental outcomes, the optimum process temperature was obtained as 65 0C, the base catalyst NaOH concentration of 0.4gm and the ratio of methanol oil was 1:6 for better results in terms of recovery of biodiesel. http://www.ijettjournal.org Page 384 International Conference on Global Trends in Engineering, Technology and Management (ICGTETM-2016) REFERENCES: [1] W.G.Wang, D.W.Lyons, M. Goutam Emissions from nine heavy trucks fueled by diesel and biodiesel blend without engine modification, Environment Science and Technology, vol. 34 (2000), pp. 933-939. [2] A.Hayyan, M.Z.Alam, M.E.S.Mirghani, N.A.Kabbashi, N.I.N.M.Hakimi, Y.M.Siran and S.Tahiruddin, Production of biodiesel from sludge palm oil by esterification process, Journal of Energy and Power engineering vol.4(1), (Jan-2011) , pp. 11-17. [3] D.M.Lapuerta, J.Rodriguez- Furnandez, Nueral network estimation of diesel particulate matter composition from transesterified waste oil blends, Fuel, vol. 84 (2005), pp. 20802085. [4] M.Hayyan,F.S.Mjalli,M.A.Hashim,I.M.Al Nashef, A Novel technique for separating glycerin from palm oil based biodieselusing ionic liquids, Fuel Process Technology , vol. 91(2010), pp. 116-120. ISSN: 2231-5381 [5] Venkata Ramesh Mamilla,M.V.Mallikarjun, Dr.G.Lakshmi Narayan Rao, Biodiesel production from palm oil by transesterification method,International Journal of Current Research,vol.4,Issue 08 (Aug-2012) pp. 083-088. [6] Singh. S & Singh.D, Renewable and sustainable energy review,biodiesel production through the use of different sources and characterization of oils and their esters as the substitute of diesel: A Review, (2009) pp. 200-216 [7] Eman N.Ali,Cadence Isis Tay, Characterization of biodiesel produced from palm oil via base catalyzed transesterification, Procedia Engineering, ELSEVIER, vol. 53(2013), pp. 7-12. [8] Novizar Nazir and Dwi Setyaningsih, Life cycle assessment of biodiesel production from palm oil and jatropha oil in Indonesia, 7th Biomass Asia Workshop [9] Yee Kian Fei, Lee Keat Teong, Palm Oil as feedstocks for biodiesel production via heterogenous transesterification: Optimization study, International Conference on Environment, 2008. http://www.ijettjournal.org Page 385