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Received June 23, 2018
Accepted October 11, 2018
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This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits
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Improvement of sugar recovery from Sida acuta (Thailand Weed) by NaOH pretreatment and application to bioethanol production
Department of Biology, Faculty of Science, Naresuan University, Muang, Phitsanulok 65000, Thailand 1Center for Agricultural Biotechnology, Faculty of Agriculture, Natural Resources and Environment, Naresuan University, Muang, Phitsanulok 65000, Thailand 2Department of Biotechnology, Sangmyung University, 20, Hongjimun 2-gil, Jongno-gu, Seoul 03016, Korea 3Department of Chemical and Biological Engineering, Korea University, 145, Anam-ro, Seongbuk-gu, Seoul 02841, Korea
kimsw@korea.ac.kr
Korean Journal of Chemical Engineering, December 2018, 35(12), 2413-2420(8), 10.1007/s11814-018-0170-1
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Abstract
Sida acuta, a common type of weed in Thailand, contains relatively high cellulose (42.7%) content. We pretreated NaOH to improve glucose recovery from S. acuta. The effect of pretreatment temperature and NaOH concentration was fundamentally investigated based on hydrolysis efficiency with recovery of solid fraction. The pretreatment condition was determined to be 3% NaOH at 60 °C for 9 h, which showed the highest glucose recovery. The hydrolysates obtained by enzymatic hydrolysis of S. acuta were applied to the fermentation of Saccharomyces cerevisiae K35, and a theoretical yield of 97.6% was achieved at 18 h. This indicated that the hydrolysates medium without detoxification had no negative effects on the fermentation. The production of biomass into bioethanol was evaluated based on the material balance of 1,000 g basis. Following this estimation, approximately 28 g and 110 g bioethanol could be produced by untreated and pretreated S. acuta, respectively, and this production was improved about 3.9 fold by NaOH pretreatment. These results again show the importance of pretreatment in biorefinery process.
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Ruangmee A, Sangwichien C, Energy Conv. Manag., 73, 381 (2013)
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Xu JL, Cheng JJ, Bioresour. Technol., 102(4), 3861 (2011)
Kim I, Han JI, Biomass Bioenergy, 46, 210 (2010)
Zhang Y, Liu YY, Xu JL, Yuan ZH, Zhuang XS, BioResources, 7, 345 (2011)
Iberahim NI, Jahim JM, Harun S, Nor MTM, Hassan O, Int. J. Chem. Eng. Appl., 3, 101 (2013)
Haque MA, Barman DN, Kim MK, Yun HD, Cho KM, J. Sci. Food Agric., 96, 1790 (2016)
Lee SH, Teramoto Y, Endo T, Bioresour. Technol., 100(1), 275 (2009)
Almeida JRM, Modig T, Petersson A, Hahn-Hagerdal B, Liden G, Gorwa-Grauslund MF, J. Chem. Technol. Biotechnol., 82(4), 340 (2007)
Klinke HB, Thomsen AB, Ahring BK, Appl. Microbiol. Biotechnol., 66(1), 10 (2004)
