CEIT, Section of Environmental Engineering, San Sebastián, Spain.
Water Res. 2009 Oct;43(18):4626-42. doi: 10.1016/j.watres.2009.07.014. Epub 2009 Jul 18.
This paper presents a new mathematical model developed to reproduce the performance of a generic sludge digester working either under aerobic or anaerobic operational conditions. The digester has been modelled as two completely mixed tanks associated with gaseous and liquid volumes. The conversion model has been developed based on a plant wide modelling methodology (PWM) and comprises biochemical transformations, physicochemical reactions and thermodynamic considerations. The model predicts the reactor temperature and the temporary evolution of an extensive vector of model components which are completely defined in terms of elemental mass fractions (C, H, O, N and P) and charge density. Thus, the comprehensive definition of the model components guarantees the continuity of elemental mass and charge in all the model transformations and between any two systems defined by the model. The aim of the generic digester model is to overcome the problems that arise when trying to connect aerobic and anaerobic digestion processes working in series or to connect water and sludge lines in a WWTP. The modelling methodology used has allowed the systematic construction of the biochemical model which acts as an initial illustrative example of an application that has been experimentally verified. The variation of the temperature is also predicted based on a thermal dynamic model. Real data from four different facilities and a straightforward calibration have been used to successfully verify the model predictions in the cases of mesophilic and thermophilic anaerobic digestion as well as autothermal thermophilic aerobic digestion (ATAD). The large amount of data from the full scale ATAD and the anaerobic digestion pilot plants, all of them working under different conditions, has allowed the validation of the model for that case study.
本文提出了一种新的数学模型,用于再现通用污泥消化器在需氧或厌氧操作条件下的性能。消化器被建模为与气态和液态体积相关的两个完全混合的罐。该转换模型是基于全厂建模方法(PWM)开发的,包括生化转化、物理化学反应和热力学考虑。该模型预测了反应器温度和模型组件的广泛向量的临时演化,这些组件完全根据元素质量分数(C、H、O、N 和 P)和电荷密度来定义。因此,模型组件的全面定义保证了在所有模型转换中和在模型定义的任意两个系统之间元素质量和电荷的连续性。通用消化器模型的目的是克服在尝试连接串联运行的好氧和厌氧消化过程或在 WWTP 中连接水和污泥线时出现的问题。所使用的建模方法允许对生化模型进行系统构建,该模型作为已通过实验验证的应用的初始说明性示例。还基于热力学模型预测了温度的变化。已经使用来自四个不同设施的实际数据和简单的校准成功验证了中温和高温厌氧消化以及自热高温好氧消化(ATAD)情况下的模型预测。来自全规模 ATAD 和厌氧消化中试工厂的大量数据,它们都在不同条件下运行,允许对该案例研究的模型进行验证。