School of Municipal and Environmental Engineering, Shenyang Jianzhu University, Shenyang, 110168, China.
State Key Laboratory of Urban Water Resource and Environment, School of Municipal and Environmental Engineering, Harbin Institute of Technology, Harbin, 150090, China.
Water Res. 2019 Sep 15;161:242-250. doi: 10.1016/j.watres.2019.05.094. Epub 2019 May 29.
IWA Anaerobic Digestion Model No. 1 (ADM1) is the most widely recognised and popular mathematical model for anaerobic digestion processes. However, the application of ADM1 to acidogenic fermentation is limited by its use of constant stoichiometry to describe the formation of products via carbohydrate fermentation. This study presents a modification of ADM1 using a variable acidogenic stoichiometric approach in which the hydrogen partial pressure (p) and pH are used to predict and regulate the acidogenic process. The fermentation of ethanol and its kinetics were introduced into the model structure. Experimental data from mixed acid-type fermentation in a 28.4 L anaerobic baffled reactor (ABR) fed with a sucrose solution with a chemical oxygen demand of 4000 mg L were used to calibrate the model parameters. Two case studies involving continuous ethanol-type fermentation in an ABR and a continuous stirring tank reactor (CSTR) were used to validate the approach. The modified model achieved good predictions of the experimental data collected from butyric acid, propionic acid, mixed acid, and ethanol-type fermentation in the ABR and CSTR using the standard ADM1 parameter values without any parameter fitting beyond implementation of the variable acidogenic stoichiometry. The p and pH thresholds in butyric acid, propionic acid, mixed acid, and ethanol-type fermentation could be predicted using this model, which was shown to be a valid mathematical tool for the regulation of fermentation type.
IWA 厌氧消化模型 No.1(ADM1)是最广泛认可和流行的厌氧消化过程数学模型。然而,ADM1 在用于产酸发酵时受到其使用恒化学计量学描述通过碳水化合物发酵形成产物的限制。本研究提出了一种使用可变产酸化学计量学方法对 ADM1 的修改,其中使用氢分压(p)和 pH 来预测和调节产酸过程。该模型结构中引入了乙醇发酵及其动力学。使用在装有化学需氧量为 4000mg/L 的蔗糖溶液的 28.4L 厌氧折流板反应器(ABR)中进行的混合酸型发酵的实验数据来校准模型参数。使用 ABR 中的连续乙醇型发酵和连续搅拌釜式反应器(CSTR)中的两个案例研究来验证该方法。使用标准 ADM1 参数值,无需进行任何参数拟合,仅通过实施可变产酸化学计量学,即可对从 ABR 和 CSTR 中的丁酸、丙酸、混合酸和乙醇型发酵中收集的实验数据进行良好的预测。可以使用该模型预测丁酸、丙酸、混合酸和乙醇型发酵中的 p 和 pH 阈值,这表明该模型是一种有效的发酵类型调节的数学工具。