Wang Liang, Liu Jianquan, Zhang Zhe, Zhang Feiyang, Ren Junli, Sun Fubao, Zhang Zhenyu, Ding Cancan, Lin Qiaowen
Sheng Wu Gong Cheng Xue Bao. 2015 Oct;31(10):1468-83.
The expensive production of bioethanol is because it has not yet reached the 'THREE-HIGH' (High-titer, high-conversion and high-productivity) technical levels of starchy ethanol production. To cope with it, it is necessary to implement a high-gravity mash bioethanol production (HMBP), in which sugar hydrolysates are thick and fermentation-inhibitive compounds are negligible. In this work, HMBP from an atmospheric glycerol autocatalytic organosolv pretreated wheat straw was carried out with different fermentation strategies. Under an optimized condition (15% substrate concentration, 10 g/L (NH4)2SO4, 30 FPU/g dry matter, 10% (V/V) inoculum ratio), HMBP was at 31.2 g/L with a shaking simultaneous saccharification and fermentation (SSF) at 37 degrees C for 72 h, and achieved with a conversion of 73% and a productivity of 0.43 g/(L x h). Further by a semi-SFF with pre-hydrolysis time of 24 h, HMBP reached 33.7 g/L, the conversion and productivity of which was 79% and 0.47 g/(L x h), respectively. During the SSF and semi-SSF, more than 90% of the cellulose in both substrates were hydrolyzed into fermentable sugars. Finally, a fed-batch semi-SFF was developed with an initial substrate concentration of 15%, in which dried substrate (= the weight of the initial substrate) was divided into three portions and added into the conical flask once each 8 h during the first 24 h. HMBP achieved at 51.2 g/L for 72 h with a high productivity of 0.71 g/(L x h) while a low cellulose conversion of 62%. Interestingly, the fermentation inhibitive compound was mainly acetic acid, less than 3.0 g/L, and there were no other inhibitors detected, commonly furfural and hydroxymethyl furfural existing in the slurry. The data indicate that the lignocellulosic substrate subjected to the atmospheric glycerol autocatalytic organosolv pretreatment is very applicable for HMBP. The fed-batch semi-SFF is effective and desirable to realize an HMBP.
生物乙醇生产成本高昂,是因为其尚未达到淀粉质乙醇生产的“三高”(高滴度、高转化率和高生产率)技术水平。为应对这一问题,有必要实施高浓度醪液生物乙醇生产(HMBP),其中糖水解产物浓度高且发酵抑制性化合物可忽略不计。在本研究中,采用不同发酵策略对常压甘油自催化有机溶剂预处理的小麦秸秆进行了HMBP。在优化条件(底物浓度15%、10 g/L硫酸铵、30 FPU/g干物质、接种比例10%(V/V))下,37℃摇瓶同步糖化发酵(SSF)72小时,HMBP产量达31.2 g/L,转化率为73%,生产率为0.43 g/(L·h)。进一步采用预水解时间为24小时的半SSF,HMBP产量达33.7 g/L,转化率和生产率分别为79%和0.47 g/(L·h)。在SSF和半SSF过程中,两种底物中90%以上的纤维素被水解为可发酵糖。最后开发了一种初始底物浓度为15%的补料分批半SSF,其中干燥底物(=初始底物重量)分为三份,在前24小时内每8小时向锥形瓶中添加一次。HMBP在72小时内产量达51.2 g/L,生产率高达0.71 g/(L·h),而纤维素转化率较低,为62%。有趣的是,发酵抑制性化合物主要是乙酸,含量低于3.0 g/L,未检测到其他抑制剂,通常存在于浆液中的糠醛和羟甲基糠醛也未检出。数据表明,经常压甘油自催化有机溶剂预处理的木质纤维素底物非常适用于HMBP。补料分批半SSF对于实现HMBP是有效且理想的。