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结合ASM1和二沉池模型组成活性污泥模拟系统,将某污水处理厂的常规检测数据转化为活性污泥系统模型所需的组分数据,然后调整模型参数,使污水处理厂出水指标最接近于污水处理厂实际数据,从而确定适合该污水处理厂的模型参数,最后对该污水处理厂的工艺参数进行了模拟改造。 相似文献
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二沉池表面负荷取值的探讨 总被引:1,自引:0,他引:1
就活性污泥法在不同系统中二沉池的设计参数如何取值进行了探讨,认为在延时曝气系统的二沉池设计中除了根据表面负荷计算之外,还应考虑固体负荷这一因素。 相似文献
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西北L市Y污水处理厂设计规模为26万m3/d,采用AAO工艺.Y污水处理厂运行过程中,发现日进水量波动较大,某典型日时变化系数按照最大时进水量/平均时进水量核算,已超过原设计总变化系数1.3.自2011年运行以来,每年冬季均发生污泥膨胀,对二沉池的稳定运行造成很大风险.通过采取超越初沉池和投加硅藻土药剂的方式,提高活性污泥无机物成分来增加其沉降性.随着进水量接近设计值,利用厂内中水系统作为冬季应急期间的二沉池,以降低现有二沉池的表面负荷,同时调整中水系统运行参数确保其出水达标,保障了Y污水处理厂的稳定运行. 相似文献
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为了探究实际工况下竖流式二沉池的流场变化及污泥质量浓度分布情况,利用RNG k-epsilon湍流模型和mixture模型,对其进行二维瞬态数值模拟,比较不同负荷、不同回流比对二沉池内部的流场变化和污泥质量浓度分布的影响。结果表明:q=0.5 m~3/(m~2·h)是竖流式二沉池比较理想的设计表面负荷;回流比对二沉池的稳定运行具有一定的影响,竖流二沉池的进口部分设计参数应当结合回流比进行适当的调整。 相似文献
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基于实际二沉池尺寸、流变性质、回流等工况,采用数值模拟方法对二沉池固液两相动力学行为进行模拟研究。结果表明,二沉池内存在多个漩涡,且分布于二沉池上部、中部和下部;混合液的流动速度在二沉池上部和污泥斗区域较低,在二沉池中下部较高;污泥高含量区分布于污泥斗及二沉池底部区域,且越靠近二沉池右侧壁面污泥层厚度不断降低。混合液流变性质模型为拟合污泥含量的赫谢尔-巴尔克莱模型时,模拟得到的速度及污泥层厚度与牛顿流体(水)模拟得到的结果较为相近且与实验结果误差不显著,但牛顿流体对二沉池底部的污泥含量预估较低,当混合液流变性质为赫谢尔-巴尔克莱模型时(与污泥含量无关)速度及污泥含量的模拟结果均较差。 相似文献
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Heung-Joe Jung Jae-Wook Lee Do-Young Choi Seong-Jin Kim Dong-Heui Kwak 《Korean Journal of Chemical Engineering》2006,23(2):271-278
The activated sludge process is one of the most frequently used processes for biological wastewater treatment. Conventional
gravity sedimentation (CGS), which is widely used as a secondary clarifier in activated sludge processes, has a routine problem
due to floating tendency, called bulking, caused by filamentous microorganisms. Dissolved air flotation (DAF) has been applied
as potential alternative to CGS as a secondary clarifier. A series of experiments were performed to measure physico-chemical
characteristics and removal efficiency of activated sludge flocs. The removal efficiency of flocs corresponding in lag and
exponential growth phases was lower, while that of flocs both in stationary and endogenous phases considerably increased.
The rise velocity of floc/bubble agglomerates was calculated by using a population balance (PB) model explaining the distribution
of floc/bubble agglomerates. The experimental results of flotation efficiency showed a similar tendency with the results predicted
by PB model for the rise velocity and distribution of floc/bubble agglomerates. It was found from our study that the DAF process
was very effective as a secondary clarifier in the activated sludge process. 相似文献
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Jeriffa De Clercq Martijn Devisscher Ivo Boonen Jacques Defrancq Peter A Vanrolleghem 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2005,80(5):523-530
A one‐dimensional clarifier model was assessed for its capability to describe dynamic full‐scale sludge concentration profiles by using the settling properties calibrated with batch settling curve data collected by a SettloMeter®. These sludge concentration profiles and batch settling tests formed part of a detailed one‐month measuring campaign on a full‐scale wastewater treatment plant; the measurements showed a daily variation in settling properties. Using the settling properties obtained from batch settling tests and a one‐dimensional model without dispersion, the dynamics of the full‐scale clarifier were analysed and the need for dispersion clearly shown. The parameters of the dispersion model were estimated from the full‐scale sludge concentration profiles. The settling properties of activated sludge can be automatically determined by fitting the model to the on‐line batch settling curve measurements and are needed as input to the one‐dimensional model. This model can therefore be used for operation and control. The dispersion model parameters have to be determined from dynamic sludge concentration profiles but are assumed to be constant for a specific clarifier. Copyright © 2005 Society of Chemical Industry 相似文献
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Muhammad Reza Saffarian Mohammad Hossein Hamedi Mehrzad Shams 《Korean Journal of Chemical Engineering》2010,27(4):1192-1204
A computational fluid dynamics model that predicts the sedimentation of activated sludge in a circular secondary clarifier with activated sludge is developed. The axisymmetric single-phase flow is simulated by using a CFD code that has been written with Intel Visual Fortran. First, sludge withdrawing by suction-lift in the near-bottom region of the clarifier is simulated using suction at the bottom of clarifier. The flow and settling processes are simulated using k-e turbulence model on a two-dimensional and orthogonal grid. A convection-dispersion equation that is extended to incorporate the sedimentation of activated sludge in the field of gravity is used. The computational domain includes the sludge blanket where the viscosity is affected by the rheological behavior of the sludge. Experimental data provided by Weiss et al. show that the relationship between shear stress and shear rate follows the Casson law for the shear rates lower than 50 s-1. Plastic viscosity of activated sludge is not removed from the concentration diffusion, so using regular non-Newtonian models leads to overestimation of blanket height. Modified Casson model is introduced to overcome the blanket height overestimation problem. Results show that the local sludge distribution in the clarifier has excellent agreement with concentration profile measurements of Weiss et al., for different treatment plant loadings. Alternative sludge withdrawing methods include withdrawing from pipes position at the bottom of clarifier and withdrawing by using sink terms in governing equations are used. Results show that the first withdrawing method gives less error comparing to these withdrawing methods. 相似文献
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An aeration process in an activated sludge plant is a continuous‐flow system. In this system, there is a steady input flow (flow from the primary clarifier or settling tank with some part from the secondary clarifier or secondary settling tank) and output flow connection to the secondary clarifier or settling tank. The experimental and numerical results obtained through batch systems can not be relied on and applied for the designing of a continuous aeration tank. In order to scale up laboratory results for field application, it is imperative to know the geometric parameters of a continuous system. Geometric parameters have a greater influence on the mass transfer process of surface aeration systems. The present work establishes the optimal geometric configuration of a continuous‐flow surface aeration system. It is found that the maintenance of these optimal geometric parameters systems result in maximum aeration efficiency. By maintaining the obtained optimal geometric parameters, further experiments are conducted in continuous‐flow surface aerators with three different sizes in order to develop design curves correlating the oxygen transfer coefficient and power number with the rotor speed. The design methodology to implement the presently developed optimal geometric parameters and correlation equations for field application is discussed. 相似文献
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Muhammad Reza Saffarian Mohammad Hossein Hamedi Mehrzad Shams 《Korean Journal of Chemical Engineering》2010,27(5):1497-1508
An axisymmetric single-phase model that predicts the sedimentation of activated sludge in a circular secondaryclarifier is
developed. The k-ɛ turbulence model is used on a two-dimensional, orthogonal and stepwise grid. The concentration equation, which is extended
to incorporate the sedimentation of activated sludge in the field of gravity, governs the mass transfer in the clarifier.
The computational domain includes the sludge blanket where the viscosity is affected by the rheological behavior of the sludge.
Results in case of non-Newtonian fluid model are compared with another numerical approach provided by Lakehal et al. Non-Newtonian
fluid models—Bingham, Casson, and Herschel-Bulkley—are used. The influence of settling velocity functions and non-Newtonian
models on the flow behavior isinvestigated. Finally, the best models are introduced and the ways that the non-Newtonian model
introduces the plastic viscosity are discussed. 相似文献
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《分离科学与技术》2012,47(7):1429-1443
Abstract Simplified mathematical models for slurry settling under quiescent conditions and in two types of upflow clarifier are presented. Effective floe radius and a coefficient in the expression for the viscosity, the only adjustable parameters, are determined by fitting to published data on settling velocities of stirred ferric hydroxide floes. These parameters are then used to calculate rates of sludge blanket rise in a reactor-clarifier operated at various flow rates. Agreement with data on ferric hydroxide floes is satisfactory. The responses of clarifiers of two different designs to transient hydraulic overloads are then calculated. The models indicate that the reactor-clarifier (fed in the middle, sludge wasted at the bottom) performs better than a clarifier which is fed at the bottom and from the middle of which sludge is wasted. 相似文献
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The theoretical densimetric Froude number values with favourable effect on the clarifier performance
The performance of secondary clarifiers is strongly related to density effects in the sedimentation vessel. The upper level of the clarifier's chamber – once considered to be inactive at the sedimentation process – now appears to play an important role in solids removal. A fully developed three-layer flow phenomenon that develops in some cases is proved to promote settling. Therefore, investigation of flow patterns at different operative conditions was carried out. Experiments were conducted in a model of a circular, centre-feed settling tank with continuous operation. Ground hazelnut shells served as the settling matter; in one set of experiments only dye was used. All laboratory runs were filmed and analysed, qualitatively and quantitatively, by means of computer-aided visualisation. The results of the study showed that a determining factor of the conditions favourable for formation of a fully developed three-layer flow is the theoretical densimetric Froude number. If the hydraulic and solid loadings are soundly chosen in accordance with these findings, the clarifier performance can be evidently improved. 相似文献
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为了研究湘潭市河东污水处理厂周进周出式二沉池的流态,利用改进的RNGk-ε双方程模型,借助FLUENT6.3软件,对不同回流比情况下的周进周出式二沉池流态进行了数值模拟.结果表明:湘潭市河东污水处理厂周进周出式二沉池并不存在短流现象;随着回流比的增大,容积利用率逐渐增大,周进周出式二沉池实际流态基本上能达到设计目的,容... 相似文献