Universidad San Francisco de Quito USFQ, Department of Chemical Engineering, Institute for Development of Alternative Energies and Materials IDEMA, Diego de Robles s/n y Av. Interoceánica, Quito D.M. 170157, Ecuador.
Bioresour Technol. 2017 Oct;241:985-992. doi: 10.1016/j.biortech.2017.06.006. Epub 2017 Jun 19.
An overall kinetic power law model has been successfully applied to study the anaerobic digestion of agricultural wastes. In this comparative kinetic study feed composition, organic load rate, residence time and process temperature have been systematically varied in an automated semi-continuous fermentation system to obtain the dependency of the rate of degradation as biogas production on the organic load rate and temperature. The results show that the overall reaction order depend only on the Chemical Oxygen Demand (COD) at values between 3.6 and 3.7. The Arrhenius approach shows a shift in the rate determining step between the mesophilic and thermophilic temperature regimes. The activation energy at the temperature insensitive mesophilic regime is very small at 8.9 (kJ/mole), while the activation energy at the temperature sensitive thermophilic regime lies around 117 (kJ/mole).
一种通用动力学幂律模型已成功应用于研究农业废弃物的厌氧消化。在这项比较动力学研究中,进料组成、有机负荷率、停留时间和过程温度在自动化半连续发酵系统中被系统地改变,以获得降解率作为沼气产量对有机负荷率和温度的依赖性。结果表明,总反应级数仅取决于化学需氧量(COD),在 3.6 到 3.7 之间。阿累尼乌斯法(Arrhenius approach)表明,在中温区和高温区之间,速率决定步骤发生了转移。在温度不敏感的中温区,活化能非常小,为 8.9(kJ/mol),而在温度敏感的高温区,活化能约为 117(kJ/mol)。