Effect of Free Fatty Acid Pretreatment to Yield, Composition and Activation Energy in Chemical Synthesis of Fatty Acid Methyl Ester

https://doi.org/10.22146/ijc.34492

Nor Saadah Mohd Alias(1), Harumi Veny(2*), Fazlena Hamzah(3), Noorhaliza Aziz(4)

(1) Faculty of Chemical Engineering, Universiti Teknologi Mara Malaysia, 40450 Shah Alam, Selangor, Malaysia
(2) Faculty of Chemical Engineering, Universiti Teknologi Mara Malaysia, 40450 Shah Alam, Selangor, Malaysia
(3) Faculty of Chemical Engineering, Universiti Teknologi Mara Malaysia, 40450 Shah Alam, Selangor, Malaysia
(4) Faculty of Chemical Engineering, Universiti Teknologi MARA, Pasir Gudang Campus, Johor Branch, Johor, Malaysia
(*) Corresponding Author

Abstract


Transesterification of waste cooking oil (WCO) for fatty acid methyl ester synthesis using calcium oxide (CaO) as a catalyst with absence and presence of free fatty acid (FFA) pretreatment (untreated and pretreated) prior to reaction have been investigated. The preliminary study was started from theoretical stoichiometric amount molar ratio of methanol to oil. This preliminary experiment showed that indeed, in transesterification with the chemical catalyst the molar ratio of methanol to oil should be exceeding the theoretical stoichiometric molar ratio, due to the fast reversible reaction. The highest FAME content of 81% was achieved at a temperature of 75 °C with pretreated FFA. The composition of methyl ester with pretreated FFA was affected by temperature, where increasing temperature leads to increasing of methyl oleate as major methyl ester in the product. The relation of temperature dependence was further studied by Arrhenius law correlation. It is shown that activation energy was affected by pretreatment of fatty acid. The activation energy (Ea) of transesterification with untreated and pretreated free fatty acid were found as ± 16 kJ/mol and ± 68 kJ/mol, respectively. Unlike untreated FFA, the Ea of transesterification with pretreated FFA was within the range of activation energy for transesterification for the base catalyst. This study showed that methyl ester synthesis was best obtained when FFA was pretreated prior to transesterification. In addition, WCO is a potential feedstock for biodiesel production since it is biodegradable, economic, environmentally friendly and abundantly available.

Keywords


biodiesel production; fatty acid methyl esters (FAME) composition; activation energy (Ea); waste cooking oil (WCO)

Full Text:

Full Text PDF


References

[1] Zhang, T., Yang, L., Zhu, Z., and Wu, J., 2002, The kinetic study on lipase-catalyzed transesterification of a-cyano-3-phenoxybenzyl alcohol in organic media, J. Mol. Catal. B: Enzym., 18 (4-6), 315–323.

[2] Demirbas, A., Bafail, A., Ahmad, W., and Sheikh, M., 2016, Biodiesel production from non-edible plant oils, Energy Explor. Exploit., 34 (2), 290–318.

[3] Adepoju, T., and Olawale, O., 2014, Acid-catalyzed esterification of waste cooking oil with high FFA for biodiesel production, Chem. Process Eng. Res., 21, 80–86.

[4] Venkateswarulu, T.C., Raviteja, C.V., Prabhaker, K.V., Babu, D.J., Reddy, A.R., Indira, M., and Venkatanarayana, A., 2014, Review on methods of transesterification of oils and fats in bio-diesel formation, Int. J. ChemTech Res., 6 (4), 2568–2576.

[5] Banković-Ilić, I.B., Stamenković, O.S., and Veljković, V.B., 2012, Biodiesel production from non-edible plant oils, Renewable Sustainable Energy Rev., 16 (6), 3621–3647.

[6] Reshad, A.S., Panjiara, D., Tiwari, P., and Goud, V.V., 2017, Two-step process for production of methyl ester from rubber seed oil using barium hydroxide octahydrate catalyst: Process optimization, J. Cleaner Prod., 142, 3490–3499.

[7] Zamberi, M.M., and Ani, F.N., 2016, Biodiesel production from high FFA rubber seed oil, ARPN J. Eng. Appl. Sci., 11 (12), 7782–7787.

[8] Ong, H.R., Khan, M.R., Chowdhury, M.N.K., Yousuf, A., and Cheng, C.K., 2014, Synthesis and characterization of CuO/C catalyst for the esterification of free fatty acid in rubber seed oil, Fuel, 120, 195–201.

[9] Ong, H.C., Silitonga, A.S., Masjuki, H.H., Mahlia, T.M.I., Chong, W.T., and Boosroh, M.H., 2013, Production and comparative fuel properties of biodiesel from non-edible oils: Jatropha curcas, Sterculia foetida and Ceiba pentandra, Energy Convers. Manage., 73, 245–255.

[10] Verma, P., and Sharma, M.P., 2016, Comparative analysis of effect of methanol and ethanol on Karanja biodiesel production and its optimisation, Fuel, 180, 164–174.

[11] Mardhiah, H.H., Ong, H.C., Masjuki, H.H., Lim, S., and Lee, H.V., 2017, A review on latest developments and future prospects of heterogeneous catalyst in biodiesel production from non-edible oils, Renewable Sustainable Energy Rev., 67, 1225–1236.

[12] Veny, H., Aroua, M.K., and Sulaiman, N.M.N., 2014, Kinetic study of lipase catalyzed transesterification of jatropha oil in circulated batch packed bed reactor, Chem. Eng. J., 237, 123–130.

[13] Gimbun, J., Ali, S., Karnwal, C.C.S.C., Shah, L.A., Hidayah, N.N., and Nurdin, S., 2013, Biodiesel production from rubber seed oil using activated cement clinker as catalyst, Procedia Eng., 53, 13–19.

[14] Xiao, Y., Gao, L., Xiao, G.M., and Lv, J., Kinetics of the transesterification reaction catalyzed by solid base in a fixed-bed reactor, Energy Fuels, 24 (11), 5829–5833.

[15] Sanjel, N., Gu, J.H., and Oh, S.C., 2014, Transesterification kinetics of waste vegetable oil in supercritical alcohols, Energies, 7, 2095–2106.

[16] Krishnakumar, U., and Sivasubramanian, V., 2017, Kinetic study of preparation of biodiesel from crude rubber seed oil over a modified heterogeneous catalyst, Indian J. Chem. Technol., 24 (4), 430–434.

[17] Maneerung, T., Kawi, S., Dai, Y., and Wang, C.H., 2016, Sustainable biodiesel production via transesterification of waste cooking oil by using CaO catalysts prepared from chicken manure, Energy Convers. Manage., 123, 487–497.

[18] Barabás, I., and Todoruţ, I.A., 2011, "Biodiesel Quality, Standards and Properties" in Biodiesel-Quality, Emissions and By-Products, Eds., Montero, G., and Stoytcheva, M., IntechOpen, 3–28.

[19] Prankl, H., Körbitz, W., Mittelbach, M., and Wörgetter, M., 2004, Review on Biodiesel Standardization World-Wide, IEA Bioenergy Task 39, Subtask: Biodiesel.

[20] Freedman, B., Butterfield, R.O., and Pryde, E.H., 1986, Transesterification kinetics of soybean oil 1, J. Am. Oil Chem. Soc., 63 (10), 1375–1380.

[21] Zhang, L., Sheng, B., Xin, Z., Liu, Q., and Sun, S., 2010, Kinetics of transesterification of palm oil and dimethyl carbonate for biodiesel production at the catalysis of heterogeneous base catalyst, Bioresour. Technol., 101 (21), 8144–8150.

[22] Van Boekel, M.A.J.S., 2008, Kinetic modeling of food quality : A critical review, Compr. Rev. Food Sci. Food Saf., 7 (1), 144–158.



DOI: https://doi.org/10.22146/ijc.34492

Article Metrics

Abstract views : 4024 | views : 4101


Copyright (c) 2019 Indonesian Journal of Chemistry

Creative Commons License
This work is licensed under a Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 International License.

 


Indonesian Journal of Chemistry (ISSN 1411-9420 /e-ISSN 2460-1578) - Chemistry Department, Universitas Gadjah Mada, Indonesia.

Web
Analytics View The Statistics of Indones. J. Chem.