Biodiesel Production Using Catalyst Na2O/Fly Ash from Waste Cooking Oil (WCO) with Transesterification Process

Article Preview

Abstract:

The consumption of fuel oil in all countries in the world is always increasing. Indonesia is one of the countries that are still dependent on fuel oil, especially for transportation and industry. Biodiesel is known as an alternative to diesel fuel that is believed to be able to overcome the problems of world energy needs. One of the raw materials that have the potential to be biodiesel is Waste Cooking Oil (WCO). This research aims to study the Na2O/Fly ash catalyst preparation process used for the transesterification reaction of WCO into biodiesel, study of purifying WCO as a raw material in biodiesel, analyze the effect of the methanol molar ratio to oil, catalyst loading and reaction time on the transesterification process in terms of the yield of the reaction, density, viscosity and an acid number of biodiesel product. The research method was begun preparation of Na2O/Fly ash catalyst and purification of WCO with despicing and neutralization methods. Afterwards, the transesterification process was running by varying %wt of the catalyst, the molar ratio of methanol to oil, and reaction time. The percentage weight of the catalyst used is 4% and 6% to the WCO weight, the molar ratio of methanol to oil is 6:1 and 8:1, and the transesterification reaction time used is 60, 80, 100 and 120 minutes. The results showed that the Free Fatty Acids (FFA) of WCO raw material was 3.102%, but after the despicing and neutralization processes were carried out, the FFA of WCO decreased to 2.538% and 0.282%, respectively. The optimal condition for the biodiesel production process was obtained when the catalyst weight is 6% with a molar ratio of methanol to oil by 8:1 which runs in 120 minutes. In these conditions, the obtained yield of reaction results are 99,09%, density 882 kg/m3, viscosity 11.15 cSt and an acid number of 0.2244 mg KOH/g. The results of XRD analysis on the catalyst Na2O/Fly ash is dominant by alumina (Al2O3), silica (SiO2), ferrous oxide (Fe2O3), calcium oxide (CaO), and natrium oxide (Na2O) compositions. Moreover, GCMS analysis on biodiesel showed that the methyl ester content formed was 98.13%. Based on parameters above, density and acid number has met the quality standards of SNI 7182: 2015.

You might also be interested in these eBooks

Info:

Periodical:

Pages:

97-105

Citation:

Online since:

December 2023

Export:

Price:

Permissions CCC:

Permissions PLS:

Сopyright:

© 2023 Trans Tech Publications Ltd. All Rights Reserved

Share:

Citation:

* - Corresponding Author

[1] Pangestu, W. and Zultiniar, Y. (2015). Catalytic cracking of palm fatty acid distillate into biofuel using palm fly ash. 1(1): p.1–5.

Google Scholar

[2] Aziz, I., Nurbayti, S. and Ulum, B. (2011). Production of biodiesel products from used cooking oil by esterification and transesterification. 2(3): p.443–448.

Google Scholar

[3] Nuraeni, N., Yun, Y. F., & Agustini, D. M. (2019). Making Biodiesel from Used Cooking Oil Using Activated Carbon Adsorbent and Making Triacetin with Nitric Acid Catalyst. Journal of Chemical Kartika, 2(1), 17–22.

Google Scholar

[4] Chai, F, Fenghua C, Fengying Z, Yang C, Xiaohong W, Zhongmin S. (2007) Transesterification of vegetable oil to biodiesel using a heteropolyacid solid catalyst. Advanced Synthesis and Catalysis. 349(7): p.1057–1065.

DOI: 10.1002/adsc.200600419

Google Scholar

[5] Xiang, Y., Xiang, Y. and Wang, L. (2017). Microwave radiation improves biodiesel yields from waste cooking oil in the presence of modified coal fly ash. Journal of Taibah University for Science. 11(6): p.1019–1029.

DOI: 10.1016/j.jtusci.2017.05.006

Google Scholar

[6] Silalahi, F. T. R. (2020). Biodiesel yang dihasilkan dari minyak sawit di Indonesia: Status dan Biodiesel yang dihasilkan dari minyak sawit di Indonesia: Status saat ini dan peluang.

DOI: 10.15408/jkv.v2i5.296

Google Scholar

[7] Kusuma, R. I., Hadinoto, J., Ayucitra, A., & Ismadji, S. (2011). Utilization of natural zeolite as a cheap catalyst in the process of making biodiesel from palm oil. 2011 National Seminar on Chemical Engineering Fundamentals and Applications.

Google Scholar

[8] Adhari, H., Yusnimar, & Putri Utami, S. (2016). UTILIZATION OF COOKING OIL INTO BIODIESEL WITH ZnO CATALYST ZINC CARBONATE PRECIPITANCY: EFFECT OF REACTION TIME. Let's FTEKNIK, 3(2), 1.

Google Scholar

[9] Wang, P., Li, L., & Wei, D. (2014). Kinetics analysis on mixing calcination process of fly ash and ammonium sulfate. Chinese Journal of Chemical Engineering, 22(9), 1027–1032.

DOI: 10.1016/j.cjche.2014.06.033

Google Scholar

[10] Martinez, L.Z., Romero, R., Natividad, R dan Gonzalez, J. 2014. Optimization of Biodiesel Production from Sunflower Oil by Transesterification Using Na2O/NaX and Methanol. Catalysis Today. 220-222:12-20.

DOI: 10.1016/j.cattod.2013.08.022

Google Scholar

[11] Alfarisa, S., Rifai, D. A., & Toruan, P. L. (2018). X-ray Diffraction Study on Zinc Oxide (ZnO) Nanostructures X-ray Diffraction Study on ZnO Nanostructures. 2(2), 53–57.

Google Scholar

[12] McCarthy, G. J., Johansen, D. M., Steinwand, S. J., & Thedchanamoorthy, A. (1987). X-Ray Diffraction Analysis of Fly ASH. Advances in X-Ray Analysis, 31, 331–342.

DOI: 10.1154/s037603080002214x

Google Scholar

[13] Wendi, Cuaca, V., & Taslim. (2014). Effect of Reaction Temperature and Catalyst Concentration for Producing Biodiesel from Waste Beef Tallow Using Heterogeneous Catalyst CaO from Waste Eggshell. Proceedings of the 5th Sriwijaya International Seminar on Energy and Environmental Science & Technology, 32–37.

Google Scholar

[14] Busyairi, M., Muttaqin, A. Z., Meicahyanti, I., & Saryadi, S. (2020). Potential of Used Cooking Oil as Biodiesel and Effect of Catalyst and Reaction Time on Biodiesel Quality Through Transesterification Process. Journal of Serambi Engineering, 5(2), 933–940.

DOI: 10.32672/jse.v5i2.1920

Google Scholar

[15] Prihanto, A., and Irawan, T.A.B. (2017), Effect of Temperature, Catalyst Concentration and Molarar Ratio of Methanol-Oil to Biodiesel Yield from Used Cooking Oil through Neutralization-Transesterification Process, Methane, Vol. 13, No. 1, pp.30-36.

Google Scholar

[16] Nengsih, D.I., Syarfi, Asmura, J. 2013. Pengaruh Rasio Molar Umpan Terhadap Metanol Dan Waktu Reaksi Proses Pembuatan Biodiesel Menggunakan Membran Reaktor. 6-9.

Google Scholar

[17] Affandi, Toni Rizki Aruan, Taslim, & Iriany. (2013). PRODUCTION OF BIODIESEL FROM BEEF FAT WITH TRANSESTERIFICATION PROCESS WITH NaOH CATALYST. USU Journal of Chemical Engineering, 2(1), 1–6.

DOI: 10.32734/jtk.v2i1.1419

Google Scholar

[18] Laksono, T. (2013). THE EFFECT OF TYPES OF NAOH AND KOH CATALYST AND THE RATIO OF FAT TO Methanol ON THE QUALITY OF BIODIESEL MADE FROM BEEF FAT. 1–19.

Google Scholar

[19] Ayetor, G., Sunnu, A., & Parbey, J. (2015). Effect of biodiesel production parameters on viscosity and yield of methyl esters: Jatropha curcas, Elaeis guineensis and Cocos nucifera. ALEXANDRIA ENGINEERING JOURNAL.

DOI: 10.1016/j.aej.2015.09.011

Google Scholar

[20] Faizal, M., Maftuchah, U., & Auriyani, W. A. (2013). THE EFFECT OF METHANOL LEVELS, Amount of CATALYST, AND REACTION TIME ON THE PRODUCTION OF BIODIESEL FROM BEEF FAT THROUGH TRANSESTERIFICATION PROCESS. x, 29–37.

Google Scholar