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Pretreatment solution recycling and high-concentration output for economical production of bioethanol

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Abstract

The purpose of this study was to enhance the economic efficiency of producing bioethanol. Pretreatment solution recycling is expected to increase economic efficiency by reducing the cost of pretreatment and the amount of wastewater. In addition, the production of high-concentration bioethanol could increase economic efficiency by reducing the energy cost of distillation. The pretreatment conditions were 95 °C, 0.72 M NaOH, 80 rpm twin-screw speed, and flow rate of 90 mL/min at 18 g/min of raw biomass feeding for pretreatment solution recycling. The pretreatment with NaOH solution recycling was conducted five times. All of the components and the pretreatment efficiency were similar, despite reuse. In addition, we developed a continuous biomass feeding system for production of high-concentration bioethanol. Using this reactor, the bioethanol productivity was investigated using various pretreated biomass feeding rates in a simultaneous saccharification and fermentation (SSF) process. The maximum ethanol concentration, yield, and productivity were 74.5 g/L, 89.5 %, and 1.4 g/L h, respectively, at a pretreated biomass loading of approximately 25 % (w/v) with an enzyme dosage of 30 FPU g/cellulose. The results presented here constitute an important contribution toward the production of bioethanol from Miscanthus.

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Acknowledgments

This study was financially supported by the Technology Development Program for Agriculture and Forestry, Ministry for Agriculture, Forestry and Fisheries, Republic of Korea (no. 309016-05).

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Authors and Affiliations

  1. Changhae Advanced Institute of Technology, Changhae Ethanol Co. Ltd, 15 Wonmansung-ro, Dukjin-gu, Jeonju, 561-203, Korea

    Minhee Han, Se-Kwon Moon & Gi-Wook Choi

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  1. Minhee Han
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  2. Se-Kwon Moon
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  3. Gi-Wook Choi
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Correspondence to Gi-Wook Choi.

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Han, M., Moon, SK. & Choi, GW. Pretreatment solution recycling and high-concentration output for economical production of bioethanol. Bioprocess Biosyst Eng 37, 2205–2213 (2014). https://doi.org/10.1007/s00449-014-1198-1

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  • DOI: https://doi.org/10.1007/s00449-014-1198-1

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