Enhanced Biodiesel and Ethyl Levulinate Production from Rice Bran through Non Catalytic In Situ Transesterification under Subcritical Water Ethanol Mixture

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In-situ transesterification method without catalysts to produce biodiesel (fatty acid ethyl esters, FAEE) from rice bran using subcritical water ethanol mixture has been investigated. This method was found to be efficient since the rice bran oil (RBO) extraction and reaction of RBO into FAEE occur simultaneously. In this process other chemical (ethyl levulinate, EL) was also formed along with FAEE. EL can be used to improve the biodiesel quality by improving the low temperature properties of biodiesel. In this study effect of co-solvent types (without co-solvent, ethyl acetate, chloroform, and n-hexane) and water ethanol ratio (20%, 40%, 50%, 60% and 80%, v/v) on the content and yield of FAEE and EL at subcritical water ethanol mixture (T= 160°C, P= 80 bar, and t= 2 h) were investigated systematically. The content and yield of FAEE and EL obtained was found to be affected by the type of co-solvent. The content of FAEE and EL obtained without co-solvent (ethanol and water polarity index were PI=5.2 and PI=10.2, respectively) and with co-solvent of ethyl acetate (PI= 4.4), chloroform (PI= 4.1) and n-hexane (PI= 0.1) were 55.80% and 3.92%, 68.63% and 1.15%, 65.56% and 2.14%, and 62.00% and 0.93%, respectively. Higher polarity index of co-solvent extracted more RBO, as consequent the yield of FAEE (79.79%) obtained was higher using ethyl acetate as co-solvent. This data also suggested that RBO contains more free fatty acids (FFA= 63.59%) rather than of triglycerides (TG= 24.94%).The content and yield of FAEE and EL decreased with increasing water ethanol ratio. The highest content of FAEE (60.57%) and EL (8.48%) and yield of FAEE (78.03%) and EL (10.92%) were obtained using water ethanol ratio of 20%, v/v.

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97-102

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July 2019

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© 2019 Trans Tech Publications Ltd. All Rights Reserved

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[1] Kim, T., Oh, Y.K., Lee, J.W., dan Chang, Y.K. (2017). Levulinate production from algal cell hydrolysis using in situ transesterification,. Algal Research. 26 : 431-435.

DOI: 10.1016/j.algal.2017.06.024

Google Scholar

[2] Knothe, G., Razon, L., (2017). Biodiesel Fuels,. Progress in Energy and Combustion Science 58 : 36–59.

DOI: 10.1016/j.pecs.2016.08.001

Google Scholar

[3] Juliano, Biemvemido O., (1985); Rice Bran, in: Rice: Chemistry and Technology, second ed., American Association of Cereal Chemists, St. Paul, MN, pp. 647e687.

Google Scholar

[4] Yucel, S Ozgul., Turkey, S., (2002). Variables affecting the yields of methyl esters derived from in situ esterification of rice bran oil". Journal of the American Oil Chemists, Society. 79, 611-614.

DOI: 10.1007/s11746-002-0531-5

Google Scholar

[5] Demirbas, A., (2011). Competitive liquid biofuels from biomass,. Appl. Energy 88 (1), 17–28.

DOI: 10.1016/j.apenergy.2010.07.016

Google Scholar

[6] Joshi, H., Moser, B.R., Toler, J., Smith, W. F., dan Walker, T., (2011). Ethyl levulinate: a potentialbio-based diluent for biodiesel which improves cold flow properties,. Biomass Bioenergy 35 (7), 3262–3266.

DOI: 10.1016/j.biombioe.2011.04.020

Google Scholar

[7] Zullaikah, S. Rahkadima, Y. T. Ju, Y. H. (2017). A non-catalytic in situ process to produce biodiesel from a rice milling by-product using a subcritical water methanol mixture,. Renewable Energy. 111, 764–770.

DOI: 10.1016/j.renene.2017.04.040

Google Scholar

[8] Hakim, A., Rohman, A. M., (2018). Concurrent production of biodiesel and chemicals from rice bran through non catalytic in situ transesterification using a subcritical water ethanol mixture,. (Undergraduate thesis).

DOI: 10.4028/www.scientific.net/msf.964.234

Google Scholar

[9] Im, H., Kim, B., Lee, J.W., (2015) . Concurrent production of biodiesel and chemicals through wet in situ transesterification of microalgae,. Bioresour. Technol. 193 : 386-392.

DOI: 10.1016/j.biortech.2015.06.122

Google Scholar

[10] Singh, V., Yadav, M., Sharma, Y.C., (2017). Effect of co-solvent on biodiesel production using calcium alumunium oxide as a reusable catalyst and waste vegetable oil,. Fuel. 203, 360–369.

DOI: 10.1016/j.fuel.2017.04.111

Google Scholar

[11] Park, Jeongseok., Kim, Bora., Chang, Yong. K., Lee, Jae W., (2017). Wet in-situ transesterification of microalgae using ethyl acetate as a co-solvent and reactant,, Bioresource Technology.

DOI: 10.1016/j.biortech.2017.01.027

Google Scholar

[12] Zullaikah, S., Rahkadima, Y. T. Ju, Y. H. (2017). A non-catalytic in situ process to produce biodiesel from a rice milling by-product using a subcritical water methanol mixture,. Renewable Energy. 111: 764–770.

DOI: 10.1016/j.renene.2017.04.040

Google Scholar

[13] Zullaikah,S. Lai, Chao-Chin,. Vali, S.R., Ju, Yi-Hsu. (2005). A Two-Step Acid Catalyzed Process for The Production of Biodiesel From Rice Bran Oil,. Bioresource Technology 96: 1889-1896.

DOI: 10.1016/j.biortech.2005.01.028

Google Scholar

[14] Taherkhani, M., Sadramelli, S.M. (2018). An Improvement and Optimization Study of Biodiesel Production from Linseed via In-Situ Transesterification using a Co-Solvent,. Renewable Energy 119:787-794.

DOI: 10.1016/j.renene.2017.10.061

Google Scholar

[15] Sakthivel,S. (2013). Influence of Co-Solvent on the Production of Biodiesel in Batch And Continuous Process,. International Journal of Green Energy: Volume 10:8, 876-884.

DOI: 10.1080/15435075.2012.727365

Google Scholar

[16] Peng,L., Lin,L., Zhang,J. (2011).Solid Acid Catalyzed Glucose Conversion to Ethyl Levulinate,. App.Catal., 259-265.

Google Scholar