Department of Chemical Engineering, University of Patras, 1 Karatheodori St., GR 26500 Patras, Greece.
Bioresour Technol. 2012 Feb;106:10-9. doi: 10.1016/j.biortech.2011.11.088. Epub 2011 Dec 3.
The present study focused on the application of the Anaerobic Digestion Model 1 on the methane production from acidified sorghum extract generated from a hydrogen producing bioreactor in a two-stage anaerobic process. The kinetic parameters for hydrogen and volatile fatty acids consumption were estimated through fitting of the model equations to the data obtained from batch experiments. The simulation of the continuous reactor performance at all HRTs tested (20, 15, and 10d) was very satisfactory. Specifically, the largest deviation of the theoretical predictions against the experimental data was 12% for the methane production rate at the HRT of 20d while the deviation values for the 15 and 10d HRT were 1.9% and 1.1%, respectively. The model predictions regarding pH, methane percentage in the gas phase and COD removal were in very good agreement with the experimental data with a deviation less than 5% for all steady states. Therefore, the ADM1 is a valuable tool for process design in the case of a two-stage anaerobic process as well.
本研究侧重于在两段式厌氧过程中,应用厌氧消化模型 1 来分析产氢生物反应器中产酸高粱提取物的甲烷生成。通过将模型方程拟合到批量实验获得的数据,估算了氢和挥发性脂肪酸消耗的动力学参数。在所有测试的水力停留时间(20、15 和 10d)下,对连续式反应器性能的模拟非常令人满意。具体而言,在水力停留时间为 20d 时,理论预测与实验数据之间的最大偏差为甲烷生成速率的 12%,而在水力停留时间为 15d 和 10d 时,偏差值分别为 1.9%和 1.1%。对于 pH 值、气相中甲烷百分比和 COD 去除,模型预测与实验数据非常吻合,所有稳定状态下的偏差均小于 5%。因此,ADM1 是两段式厌氧过程中工艺设计的一个有价值的工具。