Faculty of Chemical Engineering, Federal University of Uberlândia, Av. João Naves de Ávila, 2121, , Campus Santa Mônica - Bloco 1K, Uberlândia, MG, 38408-144, Brazil.
Bioprocess Biosyst Eng. 2021 Mar;44(3):617-625. doi: 10.1007/s00449-020-02462-x. Epub 2020 Nov 1.
Ethanol fermentation in very high gravity (VHG) saves energy consumption for ethanol distillation. As the technology offers high ethanol yield and low waste generation and it can be operated at low cost, it could be more efficient at an industrial scale than other ethanol production methods. This work studied ethanol production using a fed-batch bioreactor with a working volume of 1.5 L. The main objective of this research was evaluate the effects of temperature, sugar concentration, and cellular concentration using a Central Composite Design (CCD). Experimental conditions were selected using the surface response technique obtained from the CCD, and the results were validated to test the reproducibility. The following operating conditions were selected: temperature of 27.0 °C, sugar concentration 300.0 g/L, and cell concentration 15.0% (v/v). Under these conditions, after 30 h of fermentation the ethanol concentration, productivity and yield were 135.0 g/L, 4.42 g/(L·h) and 90.0%, respectively. All sugar was completely consumed.
在超高浓度(VHG)下进行乙醇发酵可节省乙醇蒸馏的能耗。由于该技术具有高乙醇产率、低废物生成和低成本操作的特点,因此在工业规模上可能比其他乙醇生产方法更有效。本工作使用工作体积为 1.5 L 的分批式生物反应器进行乙醇生产。本研究的主要目的是使用中心组合设计(CCD)评估温度、糖浓度和细胞浓度的影响。实验条件是使用 CCD 获得的曲面响应技术选择的,结果经过验证以测试重现性。选择了以下操作条件:温度为 27.0°C,糖浓度为 300.0 g/L,细胞浓度为 15.0%(v/v)。在这些条件下,发酵 30 小时后,乙醇浓度、生产率和得率分别为 135.0 g/L、4.42 g/(L·h)和 90.0%,所有糖均完全消耗。