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Effect of Oxalic Acid Pretreatment on Yellow Poplar (Liriodendron tulipifera) for Ethanol Production  

Kim, Hye-Yun (Dept. of Environmental Materials Science, College of Agriculture & Life Sciences, Seoul National University)
Lee, Jae-Won (Forest Products Laboratory, One Gifford Pinchod Drive)
Jeffries, Thomas W. (Forest Products Laboratory, One Gifford Pinchod Drive)
Gwak, Ki-Seob (Dept. of Environmental Materials Science, College of Agriculture & Life Sciences, Seoul National University)
Choi, In-Gyu (Dept. of Environmental Materials Science, College of Agriculture & Life Sciences, Seoul National University)
Publication Information
Journal of the Korean Wood Science and Technology / v.37, no.4, 2009 , pp. 397-405 More about this Journal
Abstract
In this study, we investigated the potential of producing bioethanol from Liriodendron tulipifera by using oxalic acid pretreatment. Amounts of fermentable sugars, mostly xylose and glucose, in the liquid fraction (hydrolysate) was $40.22g/{\ell}$ after the biomass was pretreated with 0.037 g/g of oxalic acid for 20 minutes at $160^{\circ}C$. Production amounts of ethanol was $8.6g/{\ell}$ from the 72 hours of simultaneous saccharification and fermentation (SSF) on solid fraction of the pretreated sample. At the same condition, when the reaction time increased to 40 minutes, $32.66g/{\ell}$ of fermentable sugars in the hydrolysate and $9.5g/{\ell}$ of ethanol was produced from the process of pretreatment and SSF. As a result of analyzing the fermentation inhibitors, such as acetic acid, 5-HMF, furfural and total phenolic compounds, as the reaction time increased, the amount of the fermentation inhibitors in the hydrolysate increased. Production of the fermentation inhibitors was more affected by initial concentration of oxalic acid rather than reaction time. $3.39{\sim}5.78g/{\ell}$ of acetic acid was produced by pretreatment with 0.013 g/g of oxalic acid, and the amount of furfural produced by decomposition of xylose was 2~3 times higher than the amount of 5-HMF produced by decomposition of glucose. All the hydrolysates contained more than $5g/{\ell}$ of total phenols considered as the degradation product of lignin. Therefore, by analyzing the amount of fermentable sugars and fermentation inhibitors in the hydrolysate, and producing ethanol from SSF of solid fraction of the pretreated sample, the biomass pretreated with 0.037 g/g of oxalic acid for 20 minutes at $160^{\circ}C$ can be expected to produce the most ethanol.
Keywords
yellow poplar (Liriodendron tulipifera); oxalic acid pretreatment; simultaneous saccharification and fermentation (SSF); bioethanol; hydrolysate;
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1 Allen, S. G., D. Schulman, J. Lichwa, M. J. Altal, E. Jennings, and R. Elander. 2001. A comparison of aqueos and dilute-acid-single-temperature pretreatment of yellow poplar sawdust. Ind. Eng. Chem. Res. 40(10): 2352∼2361   DOI   ScienceOn
2 Clark, T. and K. L. Mackie. 1984. Fermentation ingibitors in wood hydrolysates derived from the softwood Pinus radiate. J. Chem. Biotechnol. 34:101∼110   DOI
3 Heipieper, H. J., F. J. Weber, J. Sikkema, H. Kewelo, and J. A. M. de Bont. 1994. Mechanism of resistance of whole cells to toxic organic solvents. TIBTECH 12: 409∼415   DOI   ScienceOn
4 Kenealy, W., E. Horn, and C. Houtman. 2007. Vapor-phase diethyl oxalate pretreatment of wood chips: Part 1. Energy saving and improved pulps. Holzforschung 61: 223$\sim$229   DOI   ScienceOn
5 Larsson, S., E. Palmqvist, B. Hahn-Hägerdal, C. Tengborng, K. Stenberg, G. Zacchi, and N. Nilverbrant. 1999. The generation of fermentation inhibitors during dilute acid hydrolysis of softwood. Enzyme and Microbial Technology 24:151∼159   DOI   ScienceOn
6 Palmqvist, E. and B. Hahn-Hagerdal. 2000. Fermentation of lignocllulosic hydrolysates. II : inhibitors and mechanisms of inhibition. Bioresouce Technology 74: 25∼33   DOI   ScienceOn
7 Shimada, M., D. B. Mad, Y. Akamatsu, and T. Hattor. 1994. A proposed role of oxalic acid in wood decay systems of wood-rotting basidiomycetes. FEMS microbiol. Rev. 13: 285∼296   DOI   ScienceOn
8 Yat, S., A. Berger, and D. R. Shonnard. 2008. Kinetic characterization for dilute sulfuric acid hydrolysis of timber varieties and switchgrass. Bioresource Technology 99: 3855∼3863   DOI   ScienceOn
9 Fengel, D. and G. Wegener, 1989. Polyoses (Hemicelluloses).In: Wood: chemistry, ultrastructure, reactions. Berlin: Walter de Gruyter & Co.: pp.106∼131
10 Valerie, M. P., K. Ruel, F. Gaudard, G. Valtat, M. Petit-Conil, and B. Kurek. 2004. Oxalic acid: a microbial metabolite of interest for the pulping industry. Comptes Rendus Biologies. 327: 917∼925   DOI   ScienceOn
11 Meyer-Pinson, V., K. Ruel, F. Gaudard, G. Valtat, M. Petit-Conil, and B. Kurek. 2004. Oxalic acid: a microbial metabolite of interest for the pulping industry. Plant biology and pathology 327: 917∼925   DOI   ScienceOn
12 Saha, B. C. and M. A. Cotta. 2008. Lime pretreatment, enzymatic saccharification and fermentation of rice hulls to ethanol. Biomass and Bioenergy 32: 971∼977   DOI   ScienceOn
13 Wingre, A., M. Galbe, and G. Zacchi. 2008. Energy consideration for a SSF-based softwood ethanol plant. Bioresource Technology 99: 222∼231   DOI   PUBMED   ScienceOn
14 Teramoto, Y., S. Lee, and T. Endo. 2008. Pretreatment Pretreatment of woody and herbaceous biomass for enzymatic saccharification using sulfuric acid-free ethanol cooking. Bioresource Technology 18:8856∼8863   DOI   ScienceOn
15 Palmqvist, E., J. Almeida, and B. Hahn-Hagerdal. 1999. Mainand interaction effects of acetic acid, furfural and p-hydroxybenzoic acid on growth and ethanol productivity of yeasts. Biotechnol. Bioeng. 63: 46∼55   DOI   ScienceOn
16 Sasner, P., M. Galbe, and G. Zacchi. 2008. Technoeconomic evaluation of bioethanol production from three different lgnocellulosic materials. Biomass and Bioenergy 32: 422∼430   DOI   ScienceOn
17 Yemshanov, D. and D. McKenney. 2008. Fastgrowing poplar plantations as a bioenergy supply source for Canada. Biomass and Bioenergy 32: 185∼197   DOI   ScienceOn
18 Delgenes, J. P., R. Moletta, and J. M. Navarro. 1996. Effects of lignocellulose degradation products on ethanol fermentations of glucose and xylose by Saccharomyces cerevisiae, Zymomonas mobilis, Pichia stipitis, and Candida shehatae. Enzyme and Microbial Technology 19: 220∼225   DOI   ScienceOn
19 Shimizu, K. 1991. Chemistry of hemicelluloses. In: Wood and cellulosic chemistry. New York and Basel: Marcel Dekker, Inc.: p. 177∼214
20 Wyman, C. E. 1999. Biomass ethanol: technical progress, opportunities and commercial challenges. Annu. Rev. Eng. Environ. 24: 189∼226   DOI
21 Scalbert, A., B. Monties, and G. Janin. 1989. Tannins in wood: comparison of different estimateion methods. J. Agric. Food. Chem. 37(5): 1324∼1329   DOI
22 Heer, D. and U. Sauer. 2008. Identification of furfural as a key toxin in lignocellulosic hydrolysates and evolution of a tolerant yeast strain. Microbial Biotechnology 1 (6): 497∼506   DOI   ScienceOn
23 Ando, S., I. Arai, K. Kiyoto, and S. Hanai. 1986. Identification of aromatic monomers in steamexploded poplar and their influence on ethanol fermentation. J. Ferment. Technol. 64: 567∼570   DOI   ScienceOn
24 Pfeifer, P. A., G. Bonn, and O. Bobbleter. 1984. Influence of biomass degradation products on the fermentation of glucose to ethanol by Sacch aromyces carlsbergensis W. Biotechnol. Lett. 6:541∼546   DOI
25 Kootstra, A. M. J., N. S. Mosier, E. L. Scott, H. H. Beeftink, and J. P. M. Sanders. 2009. Differential effects of mineral and organic acids on the kinetics of arabinose degradation under lignocellulose pretreatment conditions. Biochem. Engine. J. 43: 92∼97   DOI   ScienceOn