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Optimization of Bioethanol Production from Durian Skin by Encapsulation of Saccharomyces cerevisiae
Corresponding Author(s) : N. Arlofa
Asian Journal of Chemistry,
Vol. 31 No. 5 (2019): Vol 31 Issue 5
Abstract
The optimum condition of durian skin using SSF process with encapsulation of Saccharomyces cerevisiae takes place at pH 5.0 at 37 °C. S. cerevisiae encapsulation can increase bioethanol production activity. Bioethanol production is produced at pH 4.5; 5.0 and 5.5 were 35.85, 41.25 and 39.89 g/L medium, respectively. While using free cells S. cerevisiae, bioethanol produced was 21.42, 34.94 and 28.15 g/L medium. The percentage of bioethanol produced by S. cerevisiae was 15.3 % at pH 5.0; 40.25 % at pH 4.5 and 29.43 % at pH 5.5. Encapsulation of S. cerevisiae cells can increase the resistance to process temperature by differences in bioethanol production between encapsulation with cells free of S. cerevisiae by 19.34 % at 37 °C, 24.02 % at 40 °C and 49.01 % at 45 °C. These results are higher compared to cells free of S. cerevisiae.
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References
K. Robak and M. Balcerek, Food Technol. Biotechnol., 56, 174 (2018); https://doi.org/10.17113/ftb.56.02.18.5428.
Y. Sudiyani, Utilization of Biomass Waste Empty Fruit Bunch Fiber of Palm Oil for Bioethanol Production, Jakarta, 4-5 February 2009; Research Workshop on Suistanable Biofuel, pp. 1-15 (2009).
R. Millati, C. Niklasson and M.J. Taherzadeh, Process Biochem., 38, 515 (2002); https://doi.org/10.1016/S0032-9592(02)00176-0.
K. Karimi, G. Emtiazi and M.J. Taherzadeh, Enzyme Microb. Technol., 40, 138 (2006); https://doi.org/10.1016/j.enzmictec.2005.10.046.
F. Talebnia and M.J. Taherzadeh, J. Biotechnol., 125, 377 (2006); https://doi.org/10.1016/j.jbiotec.2006.03.013.
P. Ylitervo, C.J. Franzén and M.J. Taherzadeh, J. Biotechnol., 156, 22 (2011); https://doi.org/10.1016/j.jbiotec.2011.07.018.
H.B. Aditiya, W.T. Chong, T.M.I. Mahlia, A.H. Sebayang, M.A. Berawi and H. Nur, Waste Manag., 47, 46 (2016); https://doi.org/10.1016/j.wasman.2015.07.031.
A.C. Hansen, Q. Zhang and P.W. Lyne, Bioresour. Technol., 96, 277 (2005); https://doi.org/10.1016/j.biortech.2004.04.007.
J. Khedari, N. Nankongnab, J. Hirunlabh and S. Teekasap, Build. Environ., 39, 59 (2004); https://doi.org/10.1016/j.buildenv.2003.08.001.
R. Costello and H. Chum ed.: D. Wichert, Biomassa, Bioenergy and Carbon Management, In: Bioenergy ’98: Expdaning Bioenergy Partnership p. 11-17 (1998).
K. Bélafi-Bakó, A. Koutinas, N. Nemestóthy, L. Gubicza and C. Webb, Enzyme Microb. Technol., 38, 155 (2006); https://doi.org/10.1016/j.enzmictec.2005.05.012.
B. Palmarola-Adrados, P. Chotìborská, M. Galbe and G. Zacchi, Bioresour. Technol., 96, 843 (2005); https://doi.org/10.1016/j.biortech.2004.07.004.
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N. Thongchul, S. Navankasattusas and S.-T. Yang, Bioprocess Biosyst. Eng., 33, 407 (2010); https://doi.org/10.1007/s00449-009-0341-x.
N. Kampf, Polym. Adv. Technol., 13, 895 (2002); https://doi.org/10.1002/pat.277.
Y. Kourkoutas, A. Bekatorou, I.M. Banat, R. Marchant and A.A. Koutinas, Food Microbiol., 21, 377 (2004); https://doi.org/10.1016/j.fm.2003.10.005.
M.A. Singer and S. Lindquist, Trends Biotechnol., 16, 460 (1998); https://doi.org/10.1016/S0167-7799(98)01251-7.
F.W. Bai, W.A. Anderson and M. Moo-Young, Biotechnol. Adv., 26, 89 (2008); https://doi.org/10.1016/j.biotechadv.2007.09.002.