Application of response surface methodology for optimization of waterless biodiesel production from crude palm oil

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พัชรี คำธิตา
ศศิธร หะวะนิช

Abstract

The purpose of this research was to apply the response surface methodology (RSM) based on Box Behnken design for the determination of optimum conditions on waterless biodiesel production from crude palm oil. The reaction process using acetone as co-solvent for the transesterification of palm oils in the presence of potassium hydroxide (KOH) catalyst has been developed. The relationship between the biodiesel yield as response and three operating parameters; the amount of acetone, KOH catalyst concentration and reaction temperature were analyzed by the second order regression equation. It was found that the RSM was successfully applied to analyze the interaction effects between the amount of acetone co-solvent and the reaction temperature on biodiesel yield. The optimum conditions were: 14 %wt acetone co-solvent, 1.25 %wt KOH catalyst and reaction temperature of 44 OC under a molar ratio of methanol and oils of 8:1 and a reaction time of 60 min to achieve the maximum biodiesel yield of 93.56 with the product quality factors satisfying the specification standards which were very close to the experimental values.

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How to Cite
1.
คำธิตา พ, หะวะนิช ศ. Application of response surface methodology for optimization of waterless biodiesel production from crude palm oil. Prog Appl Sci Tech. [Internet]. 2017 May 18 [cited 2024 Apr. 30];7(1):66-77. Available from: https://ph02.tci-thaijo.org/index.php/past/article/view/243112
Section
Pure and Applied Chemistry

References

Alkabbash A.N., Alam M.Z., Mirghani M.E.S., and Al-Fusaiel, A.M.A. Biodiesel Production from Crude Palm Oil by Transesterification Process. Journal of Applied Sciences. 2009. 9(17) : 3166-3170. doi:10.3923/jas.2009.3166.3170

Garnwitayee W., Kangsadan T., and Chalermwisutkul S. Conventional Homogeneous Catalytic Process with Continuous-typed Microwave and Mechanical Stirrer for Biodiesel Production from Palm Stearin. International proceedings of Chemical, Biological and Environmental Engineering, Singapore, IPCBEE 2012. 43 : 1–6.

Kusdiana D., and Saka S. Kinetics of transesterification in rapeseed oil to biodiesel fuels as treated in supercritical methanol. Fuel. 2001. 80(5) : 693-698. doi:10.1016/s0016-2361(00)00140-x

Maeda Y., Thanh LT, Imamura K, Izutani K, Okitsu K, Boi LV, et al. New technology for the production of biodiesel fuel. Green Chem. 2011. 13(5) : 1124-1128. doi:10.1039/c1gc15049a

Thanh L.T., Okitsu K., Sadanaga Y., Takenaka N, Maeda Y, and Bandow H. A new co-solvent method for the green production of biodiesel fuel – Optimization and practical application. Fuel. 2013. 103 : 742–748. doi:10.1016/j.fuel.2012.09.029

Wall J., Gerpen J. V., and Thompson, J. Soap and glycerin removal from biodiesel using waterless processes. Transactions of the ASABE. 2011. 54(2) : 535-541. doi:10.13031/2013.36456

สถาบันวิจัยวิทยาศาสตร์และเทคโนโลยีแห่งประเทศไทย (วว.). “การผลิตและการตรวจสอบมาตรฐานไบโอดีเซลเบื้องต้น.” [ออนไลน์]. เข้าถึงได้จาก : http:// www.tistr.or.th/tistr/source/techno/bio200712.pdf. (วันที่ค้นข้อมูล : 14 ตุลาคม 2558)

สถานวิจัยและพัฒนาพลังงานทดแทนจากน้ำมันปาล์มและน้ำมันพืช. คณะวิศวกรรมศาสตร์ มหาวิทยาลัยสงขลา นครินทร์. “วิธีการหาปริมาณกลีเซอรอล” [ออนไลน์]. เข้าถึงได้จาก : http://www.biodiesel.eng.psu.ac.th (วันที่ค้นข้อมูล: 14 ตุลาคม 2558)

Kamthita P., Srisuwan T. & Gesmanee S. Optimization of waterless biodiesel production from palm stearin using response surface methodology. Rangsit Journal of Arts and Sciences. 2016. 6(1) : 77-87.

Leung D.Y.C., Guo Y. Transesterification of neat and used frying oil: Optimization for biodiesel production. Fuel Processing Technology. 2006. 87(10) : 883-890. doi:10.1016/j.fuproc.2006.06.003

Eevera T., Rajendran K. and Saradha S. Biodiesel production process optimization and characterization to assess the suitability of the product for varied environmental conditions. Renewable Energy. 2009. 34(3) : 762-765. doi:10.1016/j.renene.2008.04.006