Han Minhee, Moon Se-Kwon, Choi Gi-Wook
Changhae Advanced Institute of Technology, Changhae Ethanol Co. Ltd, 15 Wonmansung-ro, Dukjin-gu, Jeonju, 561-203, Korea.
Bioprocess Biosyst Eng. 2014 Nov;37(11):2205-13. doi: 10.1007/s00449-014-1198-1. Epub 2014 May 4.
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.
本研究的目的是提高生物乙醇生产的经济效率。预处理溶液的循环利用有望通过降低预处理成本和废水量来提高经济效率。此外,高浓度生物乙醇的生产可以通过降低蒸馏的能源成本来提高经济效率。预处理条件为95℃、0.72M氢氧化钠、80rpm双螺杆转速,在以18g/min的原料生物质进料进行预处理溶液循环利用时,流速为90mL/min。用氢氧化钠溶液循环进行预处理共进行了五次。尽管重复使用,但所有成分和预处理效率均相似。此外,我们开发了一种用于生产高浓度生物乙醇的连续生物质进料系统。使用该反应器,在同步糖化发酵(SSF)过程中,以不同的预处理生物质进料速率研究了生物乙醇的生产率。在预处理生物质负载量约为25%(w/v)、酶用量为30FPU/g纤维素的情况下,最大乙醇浓度、产率和生产率分别为74.5g/L、89.5%和1.4g/L·h。本文给出的结果对芒草生物乙醇的生产做出了重要贡献。