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A plant-wide aqueous phase chemistry module describing pH variations and ion speciation/pairing in wastewater treatment process models

机译:全厂范围的水相化学模块,描述废水处理过程模型中的pH变化和离子形态/配对

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摘要

There is a growing interest within the Wastewater Treatment Plant (WWTP) modelling community to correctly describe physico–chemical processes after many years of mainly focusing on biokinetics. Indeed, future modelling needs, such as a plant-wide phosphorus (P) description, require a major, but unavoidable, additional degree of complexity when representing cationic/anionic behaviour in Activated Sludge (AS)/Anaerobic Digestion (AD) systems. In this paper, a plant-wide aqueous phase chemistry module describing pH variations plus ion speciation/pairing is presented and interfaced with industry standard models. The module accounts for extensive consideration of non-ideality, including ion activities instead of molar concentrations and complex ion pairing. The general equilibria are formulated as a set of Differential Algebraic Equations (DAEs) instead of Ordinary Differential Equations (ODEs) in order to reduce the overall stiffness of the system, thereby enhancing simulation speed. Additionally, a multi-dimensional version of the Newton–Raphson algorithm is applied to handle the existing multiple algebraic inter-dependencies. The latter is reinforced with the Simulated Annealing method to increase the robustness of the solver making the system not so dependant of the initial conditions. Simulation results show pH predictions when describing Biological Nutrient Removal (BNR) by the activated sludge models (ASM) 1, 2d and 3 comparing the performance of a nitrogen removal (WWTP1) and a combined nitrogen and phosphorus removal (WWTP2) treatment plant configuration under different anaerobic/anoxic/aerobic conditions. The same framework is implemented in the Benchmark Simulation Model No. 2 (BSM2) version of the Anaerobic Digestion Model No. 1 (ADM1) (WWTP3) as well, predicting pH values at different cationic/anionic loads. In this way, the general applicability/flexibility of the proposed approach is demonstrated, by implementing the aqueous phase chemistry module in some of the most frequently used WWTP process simulation models. Finally, it is shown how traditional wastewater modelling studies can be complemented with a rigorous description of aqueous phase and ion chemistry (pH, speciation, complexation).
机译:在多年专注于生物动力学之后,废水处理厂(WWTP)建模社区对正确描述物理化学过程的兴趣日益浓厚。确实,将来的建模需求(例如全厂磷(P)描述)在代表活性污泥(AS)/厌氧消化(AD)系统中的阳离子/阴离子行为时,需要较大但不可避免的复杂程度。在本文中,介绍了描述pH值变化以及离子形态/配对的全厂范围水相化学模块,并将其与行业标准模型连接。该模块考虑了非理想性的广泛考虑,包括离子活性而不是摩尔浓度和复杂的离子对。一般均衡被公式化为一组微分代数方程(DAE)而不是普通微分方程(ODE),以降低系统的整体刚度,从而提高仿真速度。此外,牛顿-拉夫森算法的多维版本被应用于处理现有的多个代数相互依赖关系。后者通过模拟退火方法得到了增强,以增加求解器的鲁棒性,从而使系统不再那么依赖于初始条件。模拟结果显示,当通过活性污泥模型(ASM)1、2d和3描述生物营养去除(BNR)时,比较了氮去除(WWTP1)和氮和磷去除联合处理(WWTP2)的配置下的性能,pH值预测不同的厌氧/缺氧/好氧条件。厌氧消化模型No.1(ADM1)(WWTP3)的Benchmark Simulation Model No.2(BSM2)版本也实现了相同的框架,并预测了不同阳离子/阴离子负载下的pH值。通过这种方式,通过在一些最常用的WWTP过程模拟模型中实施水相化学模块,证明了所提出方法的一般适用性/灵活性。最后,它展示了如何通过对水相和离子化学(pH,形态,络合)的严格描述来补充传统废水建模研究。

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