Makarova Ekaterina I, Budaeva Vera V, Kukhlenko Aleksey A, Orlov Sergey E
Laboratory of Bioconversion, Laboratory of Chemical Engineering Processes and Apparatuses, Institute for Problems of Chemical and Energetic Technologies, Siberian Branch of the Russian Academy of Sciences (IPCET SB RAS), Biysk, Altai Krai Russia 659322.
3 Biotech. 2017 Oct;7(5):317. doi: 10.1007/s13205-017-0964-6. Epub 2017 Sep 14.
Experiments were done to model enzymatic hydrolysis of and oat hulls treated with dilute solutions of nitric acid and sodium hydroxide in direct and reverse sequences. The enzymatic hydrolysis kinetics of the substrates was studied at an initial solid loading from 30 to 120 g/L. The effects of feedstock type and its pretreatment method on the initial hydrolysis rate and reducing sugar yield were evaluated. The fitting results by the developed models showed good agreement with the experimental data. These models designed for developing the production technology of concentrated glucose solutions can also be applied for glucose fermentation into ethanol. The initial solid loading of 60-90 g/L provides the reducing sugar concentration of 40-80 g/L necessary for ethanol synthesis. The kinetic model can also be applied to investigate enzymatic hydrolysis of other substrates (feedstock type, pretreatment method) under the similar conditions used herein, with adjusted empirical coefficient values.
进行了实验,以模拟在直接和反向顺序下用硝酸和氢氧化钠稀溶液处理的燕麦壳的酶促水解。在初始固体负载量为30至120 g/L的条件下研究了底物的酶促水解动力学。评估了原料类型及其预处理方法对初始水解速率和还原糖产率的影响。所开发模型的拟合结果与实验数据显示出良好的一致性。这些为开发浓缩葡萄糖溶液生产技术而设计的模型也可用于葡萄糖发酵生产乙醇。60-90 g/L的初始固体负载量可提供乙醇合成所需的40-80 g/L的还原糖浓度。该动力学模型还可应用于在本文所用的类似条件下,通过调整经验系数值来研究其他底物(原料类型、预处理方法)的酶促水解。