Application of numerical simulation on optimum design of two-dimensional sedimentation tanks in the wastewater treatment plant

The paper establishes the relationship between the settling efficiency and the sizes of the sedimentation tank through the process of numerical simulation, which is taken as one of the constraints to set up a simple optimum designing model of sedimentation tank. The feasibility and advantages of this model based on numerical calculation are verified through the application of practical case.

Numerical modeling method on the movement of water flow and suspended solids in two-dimensional sedimentation tanks in the wastewater treatment plant

Taking the distributing calculation of velocity and concentration as an example, the paper established a series of governing equations by the vorticity stream function method, and dispersed the equations by the finite differencing method. After figuring out the distribution field of velocity, the paper also calculated the concentration distribution in sedimentation tank by using the two dimensional concentration transport equation. The validity and feasibility of the numerical method was verified through comparing with experimental data. Furthermore, the paper carried out a tentative exploration into the application of numerical simulation of sedimentation tanks.

Impact of Untreated Sedimentation Tank Sludge Water Recycle on Water Quality During Treatment of Low Turbidity Water

The overall purpose of this research is to examine the impact of untreated sedimentation tank sludge water( USTSW) recycle on water quality during treatment of low turbidity water in coagulation—sedimentation processes. 950 m L of raw water and different concentrations of 50 m L USTSW are injected into six 1 000 m L beakers without coagulant.The results indicate that USTSW characterized as accumulated suspended solids and organic matter has active ingredients,which possess the equivalent function of coagulant. The optimal blended water turbidity is in the range of 10-20 NTU,within which USTSW recycle achieves the highest save coagulant rate. The mechanism of strengthening coagulation effect when USTSW recycle mainly depends on the chemical effect and physical effect. What is more,through scanning electron microscopy( SEM),it is found that the floc structures with USTSW recycle are more compact than those without USTSW recycle. Besides,the water quality parameters of color,NH3-N,CODMn,UV254,total aluminum,total manganese when USTSW recycle is better than the raw water without recycle,indicating that USTSW recycle can improve water quality with strengthening coagulation effect.

Experimental study and numerical simulation of the sludge concentration in a sedimentation tank

Sedimentation tanks and clarifiers play a significant role in an active sludge system, and the efficiency of the whole system is closely related with the design and operation of the sedimentation tanks. This paper focuses on the sludge concentration in each cross-section of the sedimentation tank. We measured the sludge concentration to explore its distribution inside the tank, carried in-situ tests to research the fluid pattern and real operational rules of the sedimentation tank. We also used the computational fluid dynamics (CFD) software, PHOENICS 3.5, to simulate the solid-liquid two-phase fluid inside the tank and describe the sludge concentration distribution. The numerical results indicate obviously a sludge-water interface and a compression interface inside the sedimentation tank, a stratified sedimentary region with uniform concentration and a compression region with high concentration at the bottom of the tank. Although the simulated concentrations deviated slightly from those of in-situ tests, they were still acceptable for identifying the sludge interfaces and fluid pattern inside a sedimentation tank, which are important parameters for optimizing the tank size and improving the settling efficiency.

Umbrella Labyrinth Sedimentation Device Study

Umbrella-type mud-water diversion labyrinth sedimentation device,which is characterized by the combination of two swash plate and wing plate into an umbrella type with a set angle,the angle range of the two swash plate is 15º--100º,the vertical height of the swash plate is 60-70 mm,the parallel axis of the wing plate is the vertical direction,the height is 10-20 mm.the whole adopts the modular combination mode,and can be freely combined and disassembled according to different pond design,swash plate The interval(sedimentation distance)can be freely adjusted,mud take the mud road and water take the water road,to avoid the mutual interference of the water and mud road,to achieve the stability of the water quality.The turbidity of the sedimentation pond is low,stable in 0.3-2.0 NTU.

Assessment of Seasonal Sedimentation in Rain-fed Irrigation Reservoirs by a Hillslope Erosion Modeling Approach

A distributed hillslope model is presented for the computation of seasonal sediment loads flowing into the rain-fed irrigation reservoirs (tanks) from the mountainous catchments in Sri Lanka. The model is based on the subdivision of the catchment into hillslopes and application of a sediment transport capacity equation at hillslope scale and computation of sediment loads transported to the tanks. Coarse and fine sediment loads due to hourly excess rainfall during a season are separately estimated. The model depends on fewer parameters and can be easily calibrated for a tank. The model calibration only requires measurements of coarse and fine sediment loads transported into the tank due to several rainfalls of different intensities from a representative subcatchment of the tank. Coarse sediment loads are measured by using a sediment trap installed across an ephemeral stream draining the subcatchment. Fine sediment loads are obtained by measuring the discharge and accompanied sediment concentrations over the sediment trap. The model is calibrated, verified and applied for an irrigation tank in Sri Lanka to estimate the seasonal sedimentation loads.

无线通信技术在二水厂沉淀池自动控制系统中的应用

本文主要阐述无线通信技术在净水厂排泥系统中的应用。在水厂生产过程中,应用无线AP技术,通过PLC自动控制,能够有效解决人工排泥效率差的问题。无线AP技术能够在雷雨、高温等恶劣的露天环境中为沉淀池自动控制系统提供稳定可靠的数据通信,保障水厂生产的正常连续运行。实际应用表明,该系统运行效果良好,既降低排泥用水消耗,减少人工工作量,又降低人身安全风险,为净水厂排泥系统提供了一种较好的选择方案。

基于CFD的斜板沉淀池沉淀特性分析

采用欧拉-拉格朗日方法研究了普通斜板沉淀池内水流的流态,利用单向耦合的离散项模型(DPM),计算了普通斜板沉淀池在不同工况条件下颗粒沉积特性及池内流动特性。针对普通斜板沉淀池沉淀效果差,颗粒容易再次上浮,设计了一种改良V型斜板沉淀池,并且结合标准k-ε模型,利用PISO算法,通过北京云超算中心计算了不同颗粒粒径下改良V型斜板沉淀池内颗粒运动的轨迹。结果表明:使用改良V型斜板后,颗粒物的沉降性路径减小,但是涡流强度增加,此时能量耗散更快,有利于固液分离;粒径大的颗粒也更容易沉淀。

入池流量与倾角对鱼鳃式沉沙池内水沙二相流的影响分析

为提高沉沙池的除沙效果,提出了一种新型除沙措施即鱼鳃式沉沙池。鱼鳃式沉沙池在池室内部布设多组倾斜的过滤网片,利用滤网拦截泥沙,提高泥沙沉降效率。采用物理模型试验和数值计算方法,分析不同流量和滤网角度下的流场分布和除沙效果,以此得到较优的结构型式,为该类沉沙池的工程设计和技术推广提供理论参考。结果表明,植入鱼鳃装置后沉沙池的泥沙截除率提高了12.5%~22.0%。数模计算进一步揭示,鱼鳃式沉沙池内流速变化分为五个区域,含沙量变化沿程呈现四个不同阶段。在泥沙沉积量计算中,最大泥沙沉积区出现在第一、二片滤网底部,建议增大鱼鳃装置前部的滤网孔径,使鱼鳃装置设置更加合理。

三级AO+深度处理组合工艺在中小型城镇污水厂中的应用

由于排放标准的提高和进水水质的变化,成都市某污水厂需提标改造。改造后,处理规模为2 500 m^(3)/d不变,出水水质需达到《四川省岷江、沱江流域水污染物排放标准》(DB 51/2311—2016)。本工程采用充分利用原有的生化池,改建为三级AO池并新建深度处理设施的改造方式,该改造方式节省投资、不新征用土地、抗冲击负荷强,仅需约30 min短时间碰管停水,改造后工艺运行稳定可靠,达到DB 51/2311—2016的要求(CODCr≤30 mg/L,氨氮≤1.5 mg/L,总氮≤10 mg/L,总磷≤0.3 mg/L)。项目可为中小型城镇污水厂提标改造提供借鉴经验。

大型覆土式储罐多工况强度可靠性分析

采用计算机仿真分析方法,对两种沉降方式下4种工况的覆土式储罐进行数值仿真计算,得到8种不同条件下覆土式储罐的应力应变分布云图,基于云图结果对储罐许用极限进行预测,同时进行强度与模态计算分析。计算结果显示,最大应力集中于壳体与气室连接处;由仿真模拟结果可得,计算屈服评价指标均小于实际工程要求的许用应力值,表明在8种工况下罐体满足强度要求;模态计算结果表明,覆土工况下的储罐处于稳定状态。

改良A^(2)O-臭氧-BAF工艺在地下式工业污水处理厂的设计应用

针对工业污水含特征污染物、可生化性较差,处理过程存在噪声、臭气等特点,以广东某工业园区地下式工业污水处理厂设计为例,介绍了全地埋式工业污水处理厂的进水水质特征与废水处理工艺和主要设计参数。工业污水经预处理+水解酸化+A^(2)O+高效沉淀+臭氧+BAF工艺处理后,确保出水能稳定达到《城镇污水处理厂污染物排放标准》(GB18918-2002)一级A标准。同时污水处理厂采用多种通风除臭措施,保障了操作人员的舒适度。地下式工业污水处理厂的设计不仅可以满足工业废水处理需求,而且也可以缓解用地紧张的压力,减少水厂运行过程中产生的环境风险。

南方地区9座污水厂提标工艺、造价和运营成本后评估

随着污水处理厂尾水外排标准的提高,国内污水处理厂陆续进行了提标改造。文中针对广东省同期建设的9座污水处理厂提标改造工程案例,类比了进出厂水水质、现有生化处理工艺、提标改造工艺设计参数、地下水及地质情况等,分析并总结了不同提标改造工艺选择的考虑因素;同时,根据这9座污水处理厂提标改造工程的结算情况,类比了各污水处理厂提标改造工程的费用造价指标、各工艺构筑物的土建造价指标、设备费用造价指标、其他专项费用指标等,分析并总结了不同提标改造工艺工程造价指标的大致区间范围,为今后类似污水处理厂提标改造工程设计及决策提供参考依据。

MSBR+高效沉淀池组合工艺在高排放标准下污水厂的应用

广西某污水处理厂设计能力为5×10^(4)m^(3)/d,采用10格MSBR+高效沉淀池处理工艺,出水作为环境综合整治后河道的生态补水。通过对处理水量达设计规模后的运行工况变化较大情况下的运行效果总结分析,并对超负荷运行、污泥浓度控制、出水带泥等问题提出了调控建议;实际运行数据表明,该组合工艺出水NH_(3)-N、TN、TP、SS平均消减效率分别达到99.6%、76%、97%、98.9%,主要指标甚至满足《地表水环境质量标准(GB3838-2002)》Ⅳ类水标准,具有污水处理效果稳定,耐冲击负荷强等特点,在南方丰水、雨污合流城市高排放标准污水处理方面有着较高的推广应用价值。

广东某污水处理厂氧化沟工艺提质增效改造工程设计

广东省某污水处理厂一期工程原采用氧化沟为主体的工艺,提标改造后要求出水指标达到《城镇污水处理厂污染物排放标准》(GB 18918-2002)一级A标准及《广东省地方标准水污染物排放限值》(DB44/26-2001)的第二时段一级标准的两者较严值,实际出水部分指标(如COD、SS、TP、TN)已临近排放限值,BOD_(5)、NH_(3)-N常有超标现象。提质增效工程旨在对原有生化池、消毒池等进行改造优化,并在二沉池后端新增“高效沉淀+滤布滤池”深度处理单元。提质增效后的运行数据表明,出水COD≤14 mg/L、BOD_(5)≤3.1 mg/L、ρ(TN)≤9.5 mg/L、ρ(TP)≤0.24 mg/L、ρ(SS)≤5.1 mg/L,去除率均>90%,出水水质稳定达到设计标准,同时氧化沟曝气单位能耗降低25%,单位成本低于同类型项目水平。

河道大型调蓄池泥沙冲洗方案比选研究

为减轻大型调蓄池池内泥沙淤积情况,提高调蓄池的运行效率,以深圳市南川区大沙河流域调蓄池工程为例,提出真空冲洗方案、门式冲洗方案、智能喷射器方案以及水力翻斗冲洗方案四种泥沙冲洗方案。结果表明:真空冲洗方案运行费用最低,维护最简单、安全,冲洗效果最好,使用寿命最长,且工程造价在四种方案(智能喷射器方案1350万元>门式冲洗方案910万元>真空冲洗方案810万元>水力翻斗方案600万元)中相对较低,综合考虑以上各项因素,最终选择真空冲洗方案为调蓄池的泥沙冲洗方案。

再生水厂高效沉淀池智能化控制管理的应用研究

高效沉淀池是保障城市再生水厂稳定达标,提供高品质再生水的关键工艺单元。针对其进水负荷波动大、出水要求高等特点,在规模240 m^(3)/d的中试装置上开展了高效沉淀池智能加药控制管理系统研究,开发了基于离散模型的多参数耦合PID控制策略,实现除磷药剂投加的精细化调控与管理;并在规模4.5万m^(3)/d的实际生产线开展应用,出水TP稳定低于0.30 mg/L,当目标值为0.14 mg/L时,出水正磷酸盐浓度平均为(0.13±0.02)mg/L,除磷药剂投加量节省27%。

分离沉降槽高效化改进及应用

介绍了一种高效提升分离沉降槽产能的方式,通过对分离沉降槽的槽体外部、内部的进料流程以及絮凝剂添加点的工艺优化,将分离槽产能提升约85%,清液层高度维持在9 m以上,粗液浮游物能够稳定控制在0.4 g/L以下,解决了分离沉降槽跑混的问题,提高了企业对低品位矿石的处理能力。同时5台分离沉降槽减少至3台,降低成本约20万元/a。

EBIS(改良AO)+磁混凝工艺在陕西某城市污水厂提标改造工程中的应用

陕西某城市污水处理厂总设计规模80000 m^(3)/d,其中40000 m^(3)/d生化池利用现状的CASS池进行改造,另外新建40000 m^(3)/d生化池及80000 m^(3)/d规模的深度处理设施。污水处理厂进水主要来源为城市生活污水,混合少量的工业污水,处理工艺采用“预处理+EBSI生化池+磁混凝沉淀池+次氯酸钠消毒”主体工艺,介绍了工程的工艺流程、主要设计参数及运行效果等。出水水质监测指标表明,本项目出水完全满足《陕西省黄河流域污水综合排放标准》(DB61/224-2018)中A标准。

污水厂更严格排放标准设计案例分析--以青岛市某工业园污水厂为例

青岛地区很多工业企业向乡镇集中,乡镇污水处理厂同时接纳生活污水及工业废水较为普遍。该项目近期设计规模为3000 m^(3)/d,进水中约2/3为工业废水,其中含有大量难降解污染物的多元生物废水量为300 m^(3)/d,而出水标准为准Ⅳ类(除TN外),多元生物废水采用臭氧预氧化单独处理后接入生化系统,生化段采用改良型AAO+AO工艺,TN去除全部在生物池实现,深度处理采用高效沉淀池+臭氧催化+砂滤+接触消毒工艺,项目投运后,CODCr、TN、TP去除率分别为96.38%、86.97%、98.70%,出水水质稳定达到设计标准,可为同类型污水处理厂设计提供参考。