Abstract
In recent years, increased environmental awareness and energy shortages have encouraged researchers to investigate the possibility of using alternate fuels which are environment friendly and renewable such as vegetable oils or animal fats instead of fossil fuels. Vegetable oils have considerable potential to be considered as appropriate alternative as they possess fuel properties similar to that of diesel oil. The major problem associated with direct use of vegetable oil is their high viscosity and gum content. One possible method to overcome the problem of high viscosity is the transesterification of potential vegetable oils to produce biodiesel (esters) of respective oils. This interest is because biodiesel is biodegradable, sulphur free, oxygenated and renewable alternative diesel fuel derived from vegetable oils or animal fats. In the present investigation, Mahua oil ester (biodiesel) was prepared from non-edible feedstock of Mahua raw oil. Raw Mahua oil as obtained from the market has very high value of FFA (free fatty acid) i.e. around 19%. Different samples of Mahua oil biodiesel were obtained through Transesterification process using Potassium Hydroxide (KOH) as a base catalyst, Sodium Hydroxide (NaOH) as a base catalyst and through a Two-Step Esterification & Transesterification process using Sulphuric Acid (H2SO4) and Potassium Hydroxide (KOH) as acid-base catalyst. Among the above three different methods/process, the process which reduces the FFA level to minimum was selected for further characterization and comparison of fuel properties were made for further use in C.I. Engines. In the investigation it was observed that the Two-Step Process of Esterification & Transesterification reduces the FFA level to 0.40% which was the least among other processes of transesterification which was having FFA level of 2.04% (using KOH) and 1.44% (using NaOH) respectively. The optimum process for reducing the FFA level to less than 1% was carried out with 0.33 v/v (methanol/Mahua oil) ratios and with 1.30% v/v (H2SO4/Mahua oil) ratios for acid catalyst in the first step. The above mixture of methanol and acid was mixed with preheated Mahua oil for about 1.30 h’s reaction time and at 60 °C. After completion of the first step i.e. esterification process, the mixture was allowed to settle for 1–2 h. Methanol water and biodiesel layers were formed at the top and bottom respectively and the top layer of methanol water was removed. The bottom layer was collected and the second step i.e. Transesterification was carried out with 0.25 v/v (methanol/Mahua oil) ratio and 0.75% w/v KOH as base catalyst for 1 h at 60 °C. The produced mixture was kept for settling for about 24 h and after removing glycerol from the separated layers, pure biodiesel with 98.4% yield was obtained which was washed and dried later to get pure and clean biodiesel that was found to have properties comparable to Diesel.
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References
Purusothaman P et al (2014) Effect of di tertiary butyl peroxide additive on performance and emission characteristics of biodiesel butanol blends. Int J Eng Res Technol (IJERT) 3(9):1002–1005
Yerrennagoudaru H et al (2014) Performance and emission characteristics of two cylinder diesel engine using diesel and pine oil. Int J Mod Eng Res (IJMER) 4(7):63–68
Azhari M, Faiz R, Yunus TI, Mohd Ghazi, Yaw TCS (2008) Reduction of free fatty acids in crude jatropha curcas oil via an esterification process. Int J Eng Technol 5:92–98
Kulkarni PS et al (2013) Mahua (madhuca indica) as a source of biodiesel in India. Int J Sci Eng Res 4(7):2319–2329
Ghadge SV, Raheman H (2005) Biodiesel production from mahua (madhuca indica) oil having high free fatty acids. Biomass Bioenergy 28:601–605
Atadashi IM et al (2012) Production of bio-diesel using high free fatty acid feed stocks. Renew Sustain Energy Rev 16:1–8
Nandi S (2013) Performance of C.I. engine by using bio-diesel—mahua oil. Am J Eng Res (AJER) 2(10):1–25
Demirbas A (2005) Biodiesel production from vegetable oil via catalytic and non-catalytic supercritical methanol transesterification methods. Prog Energy Combustion Sci 31:466–487
Acknowledgements
The authors acknowledge the help provided by I.C. Power Laboratory, B.I.T., Mesra, Ranchi, India for establishment of small scale biodiesel production lab and technical support by Mr. C.K. Singh, Lab In charge, I.C. Power Laboratory, B.I.T. Mesra, Ranchi, India.
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Utkarsh, Mahto, D., Kumar, A. (2017). Manufacturing of Biodiesel from Mahua (Madhuca Indica) Oil. In: Suresh, S., Kumar, A., Shukla, A., Singh, R., Krishna, C. (eds) Biofuels and Bioenergy (BICE2016). Springer Proceedings in Energy. Springer, Cham. https://doi.org/10.1007/978-3-319-47257-7_23
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DOI: https://doi.org/10.1007/978-3-319-47257-7_23
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