Effects of Weight Hourly Space Velocity and Catalyst Diameter on Performance of Hybrid Catalytic-Plasma Reactor for Biodiesel Synthesis over Sulphated Zinc Oxide Acid Catalyst
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Biodiesel synthesis through transesterification of soybean oil with methanol on hybrid catalytic-plasma reactor over sulphated zinc oxide (SO42-/ZnO) active acid catalyst was investigated. This research was aimed to study effects of Weight Hourly Space Velocity (WHSV) and the catalyst diameter on performance of the hybrid catalytic-plasma reactor for biodiesel synthesis. The amount (20.2 g) of active sulphated zinc oxide solid acid catalysts was loaded into discharge zone of the reactor. The WHSV and the catalyst diameter were varied between 0.89 to 1.55 min-1 and 3, 5, and 7 mm, respectively. The molar ratio of methanol to oil as reactants of 15:1 is fed to the reactor, while operating condition of the reactor was kept at reaction temperature of 65 oC and ambient pressure. The fatty acid methyl ester (FAME) component in biodiesel product was identified by Gas Chromatography - Mass Spectrometry (GC-MS). The results showed that the FAME yield decreases with increasing WHSV. It was found that the optimum FAME yield was achieved of 56.91 % at WHSV of 0.89 min-1 and catalyst diameter of 5 mm and reaction time of 1.25 min. It can be concluded that the biodiesel synthesis using the hybrid catalytic-plasma reactor system exhibited promising the FAME yield. Copyright © 2017 BCREC Group. All rights reserved
Received: 15th November 2016; Revised: 24th December 2016; Accepted: 16th February 2017
How to Cite: Buchori, L., Istadi, I., Purwanto, P. (2017). Effects of Weight Hourly Space Velocity and Catalyst Diameter on Performance of Hybrid Catalytic-Plasma Reactor for Biodiesel Synthesis over Sulphated Zinc Oxide Acid Catalyst. Bulletin of Chemical Reaction Engineering & Catalysis, 12 (2): 227-234 (doi:10.9767/bcrec.12.2.775.227-234)
Ma, F., Hanna, M.A. (1999). Biodiesel Production: A Review 1. Bioresou. Technol., 70: 1-15.
Vyas, A.P., Verma, J.L., Subrahmanyam, N. (2010). A Review on FAME Production Processes. Fuel, 89(1): 1-9.
Knothe, G., Sharp, C.A., Ryan, T.W. (2006). Exhaust Emissions of Biodiesel, Petrodiesel, Neat Methyl Esters, and Alkanes in a New Technology Engine. Energy and Fuels, 20(1): 403-408.
Aransiola, E.F., Ojumu, T.V., Oyekola, O.O., Madzimbamuto, T.F., Ikhu-Omoregbe, D.I.O. (2014). A Review of Current Technology for Biodiesel Production: State of the Art. Biomass and Bioenergy, 61: 276-297
Soriano, N.U., Venditti, R., Argyropoulos, D.S. (2009). Biodiesel Synthesis via Homogeneous Lewis Acid-Catalyzed Transesterification. Fuel, 88(3): 560-565.
Zhang, J., Jiang, L., (2008). Acid-Catalyzed Esterification of Zanthoxylum bungeanum Seed Oil with High Free Fatty Acids for Biodiesel Production. Bioresour Technol., 99(18): 8995-8998.
Liu, X., Xiong, X., Liu, C., Liu, D., Wu, A., Hu, Q., Liu, C. (2010). Preparation of Biodiesel by Transesterification of Rapeseed Oil with Methanol using Solid Base Catalyst Calcined K2CO3/Al2O3. J. Am. Oil Chem. Soc., 87(7): 817-823.
Srinivas, D., Satyarthi, J.K. (2011). Biodiesel Production from Vegetable Oils and Animal Fat over Solid Acid Double-Metal Cyanide Catalysts. Catal. Surv. Asia., 15(3): 145-160.
Christopher, L.P., Kumar, H., Zambare, V.P. (2014). Enzymatic Biodiesel: Challenges and Opportunities. Appl. Energy, 119: 497-520.
Kumari, V., Shah, S., Gupta, M.N. (2007). Preparation of Biodiesel by Lipase-Catalyzed Transesterification of High Free Fatty Acid Containing Oil from Madhuca indica. Energy and Fuels, 21(12): 368-372.
Al-Zuhair, S. (2005). Production of Biodiesel by Lipase-Catalyzed Transesterification of Vegetable Oils: A Kinetics Study. Biotechnol. Prog., 21(5): 1442-1448.
Micic, R.D., Tomić, M.D., Kiss, F.E., Nikolić-Djorić, E.B., Simikić, M. (2014). Influence of Reaction Conditions and Type of Alcohol on Biodiesel Yields and Process Economics of Supercritical Transesterification. Energy Convers. Manag., 86(October): 717-726.
Encinar, J.M., González, J.F., Martínez, G., Sánchez, N., Pardal, A. (2012). Soybean Oil Transesterification by the Use of a Microwave Flow System. Fuel, 95: 386-393.
Thanh, L.T., Okitsu, K., Maeda, Y., Bandow, H. (2014). Ultrasound Assisted Production of Fatty Acid Methyl Esters from Transesterification of Triglycerides with Methanol in the Presence of KOH Catalyst: Optimization, Mechanism and Kinetics. Ultrason. Sonochem., 21(2): 467-471.
Istadi, I., Yudhistira, A.D., Anggoro, D.D., Buchori, L. (2014). Electro-catalysis System for Biodiesel Synthesis from Palm Oil over Dielectric-Barrier Discharge Plasma Reactor. Bull. Chem. React. Eng. Catal., 9(2):111-120.
Buchori, L., Istadi, I., Purwanto, P., Kurniawan, A., Maulana, T.I. (2016). Preliminary Testing of Hybrid Catalytic-Plasma Reactor for Biodiesel Production using Modified-Carbon Catalyst. Bull. Chem. React. Eng. Catal., 11(1): 59-65.
Zhang, L., Sheng, B., Xin, Z., Liu, Q., 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.
Jacobson, K., Gopinath, R., Meher, L., Dalai, A. (2008). Solid Acid Catalyzed Biodiesel Production from Waste Cooking Oil. Appl. Catal. B Environ., 85(1-2): 86-91.
Talebian-Kiakalaieh, A., Amin, N.A.S., Mazaheri, H. (2013). A Review on Novel Processes of Biodiesel Production from Waste Cooking Oil. Appl. Energy, 104: 683-710.
Yan, S., DiMaggio, C., Mohan, S., Kim, M., Salley, S.O., Ng, K.Y.S. (2010). Advancements in Heterogeneous Catalysis for Biodiesel Synthesis. Top Catal., 53(11-12): 721-736.
Endalew, A.K., Kiros, Y., Zanzi, R. (2011). Heterogeneous Catalysis for Biodiesel Production from Jatropha Curcas Oil (JCO). Energy, 36(5): 2693-2700.
Furuta, S., Matsuhashi, H., Arata, K. (2006). Biodiesel Fuel Production with Solid Amorphous-Zirconia Catalysis in Fixed Bed Reactor. Biomass and Bioenergy, 30(10): 870-873.
Olivares-Carrillo, P., Quesada-Medina, J. (2012). Thermal Decomposition of Fatty Acid Chains during the Supercritical Methanol Transesterification of Soybean Oil to Biodiesel. J. Supercrit. Fluids, 72: 52-58.
Hsieh, L.S., Kumar, U., Wu, J.C.S. (2010). Continuous Production of Biodiesel in a Packed-Bed Reactor using Shell-Core Structural Ca(C3H7O3)2/CaCO3 Catalyst. Chem. Eng. J., 158(2): 250-256.
Feng, Y., Zhang, A., Li, J., He, B. (2011). A Continuous Process for Biodiesel Production in a Fixed Bed Reactor Packed with Cation-Exchange Resin as Heterogeneous Catalyst. Bioresour. Technol., 102(3): 3607-3609.
Ren, Y., He, B., Yan, F., Wang, H., Cheng, Y., Lin, L., Feng, Y., Li, J. (2012). Continuous Biodiesel Production in a Fixed Bed Reactor Packed with Anion-Exchange Resin as Heterogeneous Catalyst. Bioresour. Technol., 113: 19-22.
Da Silva, F.M., Pinho, D.M.M., Houg, G.P., Reis, I.B.A., Kawamura, M., Quemel, M.S.R., Montes, P.R., Suarez, P.A.Z. (2014). Continuous Biodiesel Production using a Fixed-Bed Lewis-Based Catalytic System. Chem. Eng. Res. Des., 92: 1463-1469.
Ketcong, A., Meechan, W., Naree, T., Seneevong, I., Winitsorn, A., Butnark, S., Ngamcharussrivichai, C. (2014). Production of Fatty Acid Methyl Esters over a Limestone-Derived Heterogeneous Catalyst in a Fixed-Bed Reactor. J. Ind. Eng. Chem., 20(4): 1665-1671.
López, D.E., Goodwin, J.G., Bruce, D.A., Lotero, E. (2005). Transesterification of Triacetin with Methanol on Solid Acid and Base Catalysts. Appl. Catal. A Gen., 295(2): 97-105.
Lawson, J.A., Baosman, A.A. (2010). Method of Electro-Catalytic Reaction to Produce Mono Alkyl Esters for Renewable Biodiesel. US Patent 7,722,755 B2 (25 May 2010).
Istadi, I., Mabruro, U., Kalimantini, B.A., Buchori, L. (2016). Reusability and Stability Tests of Calcium Oxide Based Catalyst (K2O/CaO-ZnO) for Transesterification of Soybean Oil to Biodiesel. Bull. Chem. React. Eng. Catal., 11(1): 34-39.
De Moura, C.V.R., De Castro, A.G., De Moura, E.M., Dos Santos, J.R., Moita Neto, J.M. (2010). Heterogeneous Catalysis of Babassu Oil Monitored by Thermogravimetric Analysis. Energy and Fuels, 24(15): 6527-6532.
Shibasaki-Kitakawa, N., Honda, H., Kuribayashi, H., Toda, T., Fukumura, T., Yonemoto, T. (2007). Biodiesel Production using Anionic Ion-Exchange Resin as Heterogeneous Catalyst. Bioresour. Technol., 98(2): 416-421.
Istadi, I., Anggoro, D.D., Buchori, L., Rahmawati, D.A., Intaningrum, D. (2015). Active Acid Catalyst of Sulphated Zinc Oxide for Transesterification of Soybean Oil with Methanol to Biodiesel. Procedia Environ. Sci., 23: 385-393.
Kim, S.S., Lee, H., Na, B.K., Song, H.K. (2004). Plasma-Assisted Reduction of Supported Metal Catalyst using Atmospheric Dielectric-Barrier Discharge. Catal. Today, 89(1-2): 193-200.
Zhu, X., Gao, X., Qin, R., Zeng, Y., Qu, R., Zheng, C. (2015). Plasma-Catalytic Removal of Formaldehyde over Cu – Ce Catalysts in a Dielectric Barrier Discharge Reactor. Appl. Catal. B Environ., 170-171: 293-300.
Rahimpour, M.R., Jahanmiri, A., Mohamadzadeh Shirazi, M., Hooshmand, N., Taghvaei, H. (2013). Combination of Non-Thermal Plasma and Heterogeneous Catalysis for Methane and Hexadecane Co-Cracking: Effect of Voltage and Catalyst Configuration. Chem. Eng. J., 219: 245-253.
Marlinda, M., Ramli, R., Irwan, M. (2015). A Comparative Study of Catalityc Activity of Heterogeneous Base of Banana Stem Ash and Fly Ash on Production of Biodiesel by Ultrasonic Silica. Int. J. Sci. Technol. Res., 4(8): 169-172.
Chen, M., Mihalcioiu, A., Takashima, K., Mizuno, A. (2009). Catalyst Size Impact on Non-Thermal Plasma Catalyst Assisted deNOx Reactors. Proceeding 11th Int. Conf. Electrost. Precip. 1: 681-684.
Chen, M.G., Chen, J., Liao, X., Cui, C., Yu, D.X., Rong, J.F., Zhang, F. (2011). The Effect of Catalyst Sizes on Discharge Power in Dielectric Barrier Discharge Reactor. ICMREE2011 - Proc. 2011 Int. Conf. Mater. Renew. Energy Environ., 2: 1413-1417
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