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Development and calibration of bio-kinetic models for organic carbon and nitrogen biodegradation in an aerobic activated sludge system

机译:需氧活性污泥系统中有机碳和氮生物降解的生物动力学模型的开发和校准

摘要

Substrate removal mechanisms in a mixed culture of an activated sludge system are still a mystery that researchers have been trying to unravel by proposing anddeveloping models to interpret the observed experimental data. Activated Sludge Model Number 1 (ASM1) was first introduced to better understand the biochemicalmechanisms during carbon and nitrogen oxidation and was based on the assumption that the external substrate is consumed only for biomass growth. This model ignoredthe formation of intracellular polymers (storage products) in the biomass cell, though several researchers observed the phenomenon of storage of carbon sources and thesignificant role it played in the carbon removal process. As a consequence, the Activated Sludge Model Number 3 (ASM3) was formulated assuming that all the easily biodegradable substrate is first stored internally during the feast phase before being used for growth during famine conditions. However, experimental observations proved that both storage and growth occur simultaneously during thefeast phase. Consequently, the simultaneous storage and growth (SSAG) model was developed as an extension to ASM3 specifically to gain an in-depth understanding ofthe carbon oxidation process.While considerable investigation has been focused on model calibration using respirometric measurements of the oxygen uptake rate (OUR) during the aerobic biodegradation of substrate, model-based interpretation of titrimetric measurements has been limited. In biological systems, the oxygen consumption and correspondingpH changes occur simultaneously and can be easily monitored using respirometric and titrimetric experimental observations respectively. Attempts were, therefore,made to calibrate ASM1 using titrimetric measurements. During the subsequent successful development, consideration was given to the pH effects of carbon uptake,ammonia uptake for growth, CO2 production from carbon metabolism and the nonlinear carbon dioxide transfer rate (CTR) due to stripping. While respirometry was successfully used to calibrate every proposed new model, the interpretation of titrimetric measurements, however, was always based on ASM1, using calibration substrates such as acetate and ammonium. The SSAG model, developed in the year2005, proposed an improved kinetic expression for the degradation of storage products under famine conditions. It was successfully calibrated using on-line respirometric measurements and validated using off-line storage productsmeasurements with acetate used as a calibration substrate. However it failed to explain the titrimetric behavior of the substrate biodegradation process. While in most cases the above models were calibrated using simple synthetic substrates, the application of these models for complex substrates was not investigated.Therefore, in this dissertation, the biodegradation kinetics for different substrates like acetate (simple carbon source), sodium dodecyl sulfate (relatively complex carbon source), ammonium (simple nitrogen source), urea (relatively complex nitrogen source) and glutamic acid (combination of carbon and nitrogen) were investigated. Atitrimetric respirometer, established in the Water-waste laboratory in the Faculty of Engineering and Surveying, University of Southern Queensland, Australia, was usedto conduct batch experiments in order to monitor substrate biodegradation process in an aerobic activated sludge system. Both the dissolved oxygen and the pH controldata were logged with the Labview software package. A spreadsheet program was used to calculate the oxygen uptake rate and the proton production/consumption ratefrom the raw measurements.During batch experiments, the biodegradation of all five test substrates showed unique respirometric and titrimetric behaviors indicating that each of these compounds is biodegraded using distinctive mechanisms with the involvement and coordination of different bacterial populations. The pattern of OURs were observedvarying from substrate to substrate describing the characteristics of test compounds. The titrimetric profiles were also different for different substrates biodegradationreflecting the on-going biochemical reaction of respective substrate in activated sludge system. While acetate biodegradation, for example, caused protonconsumption (at pH 7.8) in the liquid medium, proton production was noted under feast conditions when either sodium dodecyl sulfate or glutamic acid was used as atest substrate.An in-depth revision of the existing activated sludge models was completed and the models were assessed using experimental observations. An improved bio-kineticmodel which includes both the oxygen and proton balances for the biodegradation of each of the test substrates was then developed. In addition, the substratesbiodegradation pathway and the non-linear CO2 transfer process were considered during the modeling. For proper model evaluation, the proposed model was calibrated using varying initial substrate concentrations and pH levels. In addition, three different calibration approaches: using respirometric measurements alone, using titrimetric measurements alone and using combined respirometric-titrimetric measurements, were applied during the study. The estimation of model parameters was undertaken using non-linear techniques utilizing the algorithms in theoptimisation toolbox (MATLAB).For the biodegradation of each test substrate, the proposed model was successfully calibrated using both the respirometric and titrimetric behaviors in the activatedsludge system. The estimated model parameters showed consistent results for all three calibration approaches thereby confirming the precision of the proposed model.The parameter estimation errors (calculated for 95% confidence intervals) as well as the mean squared errors for the different calibration approaches were quitereasonable and confirmed the statistical soundness of the proposed model. In addition, the proposed model was validated using off-line measurements.This dissertation presents an in-depth explanation of how the proposed models interpret the biodegradation processes and how the model parameters vary for different substrates in an activated sludge system. The results will be helpful in further refining current models that can contribute to the optimization of the design operation and enhanced performance of full scale wastewater treatment plants.
机译:活性污泥系统的混合培养物中的底物去除机制仍然是一个谜,研究人员一直试图通过提出和开发模型来解释观察到的实验数据来揭开谜底。最初引入1号活性污泥(ASM1)是为了更好地理解碳和氮氧化过程中的生化机制,并且基于以下假设:外部底物仅用于生物质生长。该模型忽略了生物质细胞中细胞内聚合物(存储产物)的形成,尽管一些研究人员观察到了碳源的存储现象及其在碳去除过程中所起的重要作用。因此,假设所有易于生物降解的基质首先在盛宴阶段内部存储,然后在饥荒条件下用于生长,那么就制定了3号活化污泥模型(ASM3)。然而,实验观察证明,在盛宴期,贮藏和生长同时发生。因此,开发了同时存储和生长(SSAG)模型作为对ASM3的扩展,专门用于深入了解碳氧化过程。尽管相当多的研究都集中在使用呼吸吸收法测量氧气吸收率的模型校准上(本店)在基质的好氧生物降解过程中,滴定法测量的基于模型的解释受到限制。在生物系统中,耗氧量和相应的pH变化会同时发生,并且可以分别使用呼吸测定法和滴定法实验观察值进行轻松监测。因此,尝试使用滴定法测量来校准ASM1。在随后的成功开发过程中,考虑了碳吸收的pH效应,氨吸收的增长,碳代谢产生的CO2以及汽提引起的非线性二氧化碳转移速率(CTR)。虽然呼吸测定法已成功用于校准每个提出的新模型,但是滴定度测量的解释始终基于ASM1,并使用诸如乙酸盐和铵盐之类的校准底物。 SSAG模型于2005年开发,为饥荒条件下的存储产品降解提供了改进的动力学表达。它已使用在线呼吸测定法成功校准,并使用了以乙酸盐为校准底物的离线存储产品测量法进行了验证。然而,它不能解释底物生物降解过程的滴定行为。尽管在大多数情况下上述模型是使用简单的合成底物进行校准的,但并未研究这些模型在复杂底物上的应用。因此,在本文中,本文研究了不同底物如乙酸盐(简单碳源),十二烷基硫酸钠(研究了相对复杂的碳源),铵(简单的氮源),尿素(相对复杂的氮源)和谷氨酸(碳和氮的组合)。在澳大利亚南昆士兰大学工程与测量学院的废水实验室中建立的滴定呼吸仪用于进行批处理实验,以监测需氧活性污泥系统中基质的生物降解过程。溶解氧和pH控制数据均通过Labview软件包记录。使用电子表格程序从原始测量值计算氧气吸收率和质子产生/消耗率。在批处理实验中,所有五种测试底物的生物降解均表现出独特的呼吸和滴定行为,表明每种化合物均采用独特的机理进行了生物降解。在不同细菌种群的参与和协调下。从底物到底物观察到的OURs模式各不相同,描述了测试化合物的特性。对于不同的底物生物降解,滴定曲线也不同,这反映了活性污泥系统中各个底物的持续生化反应。例如,醋酸盐的生物降解会导致液体介质中的质子消耗(pH 7.8),但在盛宴条件下(使用十二烷基硫酸钠或谷氨酸作为测试底物时)会注意到质子的产生。对现有活性污泥的深入研究完成模型并使用实验观察评估模型。然后,开发了一种改进的生物动力学模型,该模型包括用于每个测试底物生物降解的氧和质子平衡。此外,在建模过程中考虑了底物的生物降解途径和非线性CO2转移过程。为了进行适当的模型评估,建议的模型使用不同的初始底物浓度和pH值进行校准。此外,在研究过程中采用了三种不同的校准方法:单独使用呼吸测量,单独使用滴定测量以及组合使用呼吸-滴定测量。使用优化工具箱(MATLAB)中的算法,使用非线性技术对模型参数进行估算。对于每种测试底物的生物降解,使用活性污泥系统中的呼吸行为和滴定行为,成功地对提出的模型进行了校准。估计的模型参数显示了所有三种校准方法的一致结果,从而证实了所提出模型的精度。参数估计误差(针对95%置信区间计算)以及不同校准方法的均方误差均相当合理,并确认了建议模型的统计稳健性。此外,本文提出的模型通过离线测量得到了验证。本文对提出的模型如何解释生物降解过程以及活性污泥系统中不同基质的模型参数如何变化进行了深入的解释。该结果将有助于进一步完善当前的模型,这些模型可有助于优化设计操作并增强大型废水处理厂的性能。

著录项

  • 作者

    Hoque Muhammad A.;

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  • 年度 2010
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  • 原文格式 PDF
  • 正文语种 {"code":"en","name":"English","id":9}
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