电除尘器阳极板振打加速度分布规律与仿真设计

应用有限元分析软件LS-DYNA对影响电除尘器阳极板振打效果的锤头质量、锤臂长、悬挂方式及极板厚度等因素进行了数值仿真,分析了各因素对阳极板振打加速度分布的影响;利用分析结果对振打装置的结构进行了改进设计,结果表明可以较好地满足工业除尘的要求。本研究提出的电除尘器阳极板振打仿真方法为电除尘器振打装置的参数设计提供了一条新的途径。     

基于非稳态静电收尘理论的电除尘器运行参数的研究

为了进一步提高电除尘器的收尘效率,满足国家新的烟尘排放标准,依据研究建立的非稳态静电收集理论,提出了电除尘器供电电压及振打周期的优化措施.非稳态静电收尘理论研究与实验研究表明,收尘效率对供电电压存在一最大值,且此最佳供电电压是随极板沉积粉尘层比电阻、粉尘层厚度等动态变化的;振打周期的长短与粉尘层比电阻有关.据此提出的运行参数优化结果表明,对于比电阻不同的粉尘,电除尘器收尘效率最高时对应的供电电压随粉尘层比电阻的增大而降低,对于同一粉尘,最佳供电电压随粉尘层厚度的增长而提高;粉尘层比电阻低于1011Ω·cm时,一般保持极板粉尘层厚度在3～5 mm以内为佳,对于高比电阻粉尘应寻求适宜的清灰方式保障极板处于清洁状态.     

Al／C／Fe复合电极电絮凝法同时除氟除砷（V）

为了同时去除地下水中的氟和砷，提出了Al／C／Fe复合电极电絮凝法和Al／C—Fe／C依次除氟砷法，并进行效果对比。研究了Al／C／Fe复合电极电絮凝法的影响因素，并对复合电极电絮凝产生的絮体进行了SEM-EDX分析。结果表明，Al／C／Fe复合电极电絮凝法对氟、砷的去除速率分别是Al／C-Fe／C依次除氟砷法的1．43倍和4．73倍；初始氟／砷浓度为4．0／1．0、4．0／0和0／1．0mg／L3种条件下，通过铝极板、铁极板的电流密度均为0．10mA／cm2时，达到最好的除氟除砷效果，与初始氟／砷浓度无关。     

Al/C/Fe复合电极电絮凝法同时除氟除砷(Ⅴ)简

为了同时去除地下水中的氟和砷，提出了Al/C/Fe复合电极电絮凝法和Al/C-Fe/ C依次除氟砷法，并进行效果对比。研究了Al/C/Fe复合电极电絮凝法的影响因素，并对复合电极电絮凝产生的絮体进行了SEM-EDX分析。结果表明，Al/C/Fe复合电极电絮凝法对氟、砷的去除速率分别是Al/C-Fe/C依次除氟砷法的1.43倍和4.73倍；初始氟/砷浓度为4.0/1.0、4.0/0和0/1.0 mg/L 3种条件下，通过铝极板、铁极板的电流密度均为0.10 mA/cm²时，达到最好的除氟除砷效果，与初始氟/砷浓度无关。     

双区静电除尘器的除尘效率影响因素和理论公式研究

研究了预荷电压、烟气流速、极板间距和电极型式对双区静电除尘器除尘效率的影响,推导了双区静电除尘器的除尘效率理论公式,并与实验值和多依奇公式计算值进行了对比验证。结果表明,双区静电除尘器的除尘效果好于单区静电除尘器,其最佳工况是预荷电压25kV,烟气流速0.50m/s,极板间距400mm,采用芒刺电极。推导得到的双区静电除尘器的除尘效率理论公式不仅收尘电压较低时与实际情况相符,而且收尘电压较高时也与实际情况基本吻合,比多依奇公式更能反映双区静电除尘器的除尘效率。     

滚筒式生物反应器的设计及应力分析

针对城市生活垃圾好氧堆肥的处理工艺，设计一种用于好氧堆肥的滚筒式生物反应器。滚筒式生物反应器的设计主要包括主体结构设计，及反应器主体结构强度模拟分析。应用赫兹接触理论对支承装置中滚圈与托轮之间的接触应力进行计算。同时，结合ANSYS中不分离的接触方式模拟分析支承装置的接触应力，得出支承装置接触应力的分布规律，并将理论计算结果与ANSYS模拟结果进行对比。     

道路交通噪声预测模式预测结果的比较

为了分析实际环境影响评价中常用的各种公路交通噪声预测模型预测结果之间存在的差异,并验证各预测方式与实测值之间的相符性,通过对选取的高速公路和市政快速公路采用各种预测模型计算比较,并用实际监测值对各模型预测结果进行验证,结果发现,不同的预测方式会造成预测结果之间昼间4～9 dB、夜间5～10 dB的差异,采用2006版规范计算车速和单车噪声源强,距离衰减考虑车流量大小的预测方式得到的预测结果与实测值最为接近。     

电沉积处理电解锌漂洗废水的实验研究

采用电沉积技术对电解锌漂洗废水进行初步处理，以求达到废水回用和重金属锌的回收。研究了电沉积法处理含锌废水过程中各个影响因素对电沉积效果的影响，并且设计了正交实验。结果表明，极板间距、槽电压、进水pH、极板材料等对二维电沉积处理模拟废水具有显著影响。适宜的电沉积条件是：极板间距20 mm、槽电压5～6 V、阴极板材料为铝板、电沉积时间为30～45 min。     

非线性回归法计算曝气设备清水氧传递系数

分析对比作图法、线性回归法和非线性回归法计算曝气设备清水氧传递系数(KLa)各自的优缺点。指出在实际测定曝气设备性能中,使用非线性回归法计算KLa更加可靠．而且可以使测试过程更加容易控制。所以在实际测试过程中,推荐使用非线性回归法计算KLa。     

电絮凝处理三次采油废水

采用电絮凝技术对含PAM的三次采油废水进行处理,研究了不同极板、pH、电流密度、极板间距、搅拌速度、反应时间以及极性交换周期对大庆三次采油废水处理效果的影响。通过处理效果和成本分析,铝作为极板时处理效果要优于铁板,最佳实验条件下COD去除率达到了94.6%。同时对三次采油废水的主要性质和电絮凝处理三次采油废水的作用机理进行了分析,发现COD主要通过絮凝沉降作用去除,而电化学氧化作用和气浮作用对COD的去除效果并不显著。与普通化学混凝法相比,电絮凝处理三次采油废水在处理效果和成本方面有着独特的优势。     

可旋转径向式微粒捕集器消声特性影响因素灰色关联分析

为降低可旋转径向式微粒捕集器中的排气噪声,采用有限元法建立可旋转径向式微粒捕集器声学特性模型,分析得到了其消声特性和传递损失曲线,并采用灰色关联分析方法研究可旋转径向式微粒捕集器结构参数对消声特性的影响程度。结果表明,可旋转径向式微粒捕集器具有降噪能力,且对高频噪声消声效果明显好于低频噪声,平均消声量为20 dB左右;直径比和扩张管锥角是影响可旋转径向式微粒捕集器消声特性的2个主要因素,适当选用小的直径比和扩张管锥角,有利于提高可旋转径向式微粒捕集器的消声性能。     

Intercomparison between TRIO-EF and IMPACT codes with reference to experimental strontium migration data

This work presents an intercomparison exercise between two geochemical migration codes, TRIO-EF (an object-oriented finite element code) and IMPACT (a chemical engineering code using mixing cells in series). The predictions of the two codes are compared with the reference experimental results obtained in a previous study of strontium transport in soil columns. This simulated geochemical system is well documented and includes ion exchange and dissolution-precipitation reactions. The solution transport is simulated by a one-dimensional advection-dispersion model. The predictions of TRIO-EF and IMPACT are both in good agreement with the experimental results. However, slight differences can be observed between the two codes, especially when concentration discontinuities are involved, such as precipitation fronts or changes in boundary conditions. These discrepancies between the two codes can mainly be attributed to the different discretisation approaches.     

One-dimensional simulation of solute transfer in saturated-unsaturated porous media using the discontinuous finite elements method

A one-dimensional transport model for simulating water flow and solute transport in homogeneous-heterogeneous, saturated-unsaturated porous media is presented. The model is composed of a combination of accurate numerical algorithms for solving the nonlinear Richard's and advection-dispersion equations (ADE). The mixed form of Richard's equation is solved using a standard finite element method (FEM) with primary variable switching. The transport equation is solved using operator splitting, with the discontinuous finite element method (DFE) for discretization of the advective term. A slope limiting procedure for DFE avoids numerical instabilities but creates very limited numerical dispersion for high Peclet numbers. An implicit finite differences scheme (FD) is used for the dispersive term. The unsaturated flow and transport model (Wamos-T) is applied to a variety of rigorous problems including transient flow, heterogeneous medium and abrupt variations of velocity in magnitude and direction due to time-varying boundary conditions. It produces accurate and mass-conservative solutions for a very large range of grid Peclet numbers. The Wamos-T model is a good and robust alternative for the simulation of mass transport in unsaturated domain.     

One-dimensional simulation of solute transfer in saturated–unsaturated porous media using the discontinuous finite elements method

A one-dimensional transport model for simulating water flow and solute transport in homogeneous–heterogeneous, saturated–unsaturated porous media is presented. The model is composed of a combination of accurate numerical algorithms for solving the nonlinear Richard's and advection–dispersion equations (ADE). The mixed form of Richard's equation is solved using a standard finite element method (FEM) with primary variable switching. The transport equation is solved using operator splitting, with the discontinuous finite element method (DFE) for discretization of the advective term. A slope limiting procedure for DFE avoids numerical instabilities but creates very limited numerical dispersion for high Peclet numbers. An implicit finite differences scheme (FD) is used for the dispersive term.The unsaturated flow and transport model (Wamos-T) is applied to a variety of rigorous problems including transient flow, heterogeneous medium and abrupt variations of velocity in magnitude and direction due to time-varying boundary conditions. It produces accurate and mass-conservative solutions for a very large range of grid Peclet numbers. The Wamos-T model is a good and robust alternative for the simulation of mass transport in unsaturated domain.     

Development and analysis of an adaptive transport scheme

An approach to solving the advection dominated atmospheric mass transport problem which adaptively constructs and updates the computational mesh is implemented and analyzed. The formulation of the mesh adaptation algorithm allows for information from other model processes as well as transport to influence mesh refinement. Comparisons to other methods are limited to a pure advection test problem. The scheme is based on a Petrov–Galerkin finite element method using quadratic interpolating polynomials over triangular elements. The temporal component of the transport equation is discretized using the Crank–Nicolson method. A single time step is applied to the entire domain regardless of mesh refinement levels. Two means of upwind biasing the solution via modification of the finite element weighting functions are investigated. Criteria for refining and unrefining the mesh based on advective flux and an estimate of the error are proposed and compared. The effects of varying the number of time steps taken between mesh refinements are analyzed. Results for adapted mesh solutions of a test problem are shown to be superior to corresponding uniform mesh finite element solutions. Comparisons to several other popular uniform mesh advection schemes indicate either equal or improved accuracy for the adapted mesh solutions.     

Effect of temperature, gas phase composition, pH and microbial activity on As, Zn, Pb and Cd mobility in selected soils in the Ebro and Meuse Basins in the context of global change

This study estimates the effect of environmental parameters on the mobility of four inorganic contaminants (As, Zn, Pb and Cd) in soils from three areas in the Ebro and Meuse River basins, within the context of global change. An experimental method, applicable to various soil systems, is used to measure the effect of four global-change-sensitive parameters (temperature, gas phase composition, pH and microbial activity). The aqueous phase of batch incubations was sampled regularly to monitor toxic element concentrations in water. Statistical processing enabled discrimination of the most relevant variations in dissolved concentrations measured at different incubation times and under different experimental conditions. Gas phase composition was identified as the most sensitive parameter for toxic element solubilization. This study confirms that total soil concentrations of inorganic pollutants are irrelevant when assessing the hazard for ecosystems or water resource quality.     

有限单元法及其在河流污染计算中的应用

介绍了应用有限单元法预测计算河道较平直，水流稳定河流中污染物浓度分布的二维平面数学模型，该模型具有应用方便，计算迅捷等优点，计算中无须先知道排放口污染物掺混浓度，能直观地反映有多个排放口的河流中的污染物浓度分布的情况。     

罐底含油泥热解动力学参数计算方法的优选

在化学反应设计中反应动力学是较重要的因素。为得到更合理的污泥热解动力学参数计算方法,利用热重分析仪,在氮气气氛下对罐底含油污泥的热解特性进行研究。根据热重实验数据,分别采用Coats-Redfern法、Kissinger法、FWO法和Popescu法计算污泥热解动力学参数,并获取罐底泥热解制油的主要阶段(第2阶段)的反应活化能E、频率因子A并分析各种方法反应机理。通过对比不同计算方法得到动力学参数及拟合曲线与实验曲线的相关性,确定了最佳罐底含油污泥热解动力学参数计算方法。研究表明,Popescu法得到罐底泥的热解过程符合Jander方程,活化能E为101.43 kJ/mol,与FWO法得到的91.20 kJ/mol相近,且预测曲线与实验曲线有较好的相关性(0.9816),说明Popescu法计算罐底泥热解动力学参数更合适。     

A new tracer technique for monitoring groundwater fluxes: the Finite Volume Point Dilution Method

Quantification of pollutant mass fluxes is essential for assessing the impact of contaminated sites on their surrounding environment, particularly on adjacent surface water bodies. In this context, it is essential to quantify but also to be able to monitor the variations with time of Darcy fluxes in relation with changes in hydrogeological conditions and groundwater - surface water interactions. A new tracer technique is proposed that generalizes the single-well point dilution method to the case of finite volumes of tracer fluid and water flush. It is called the Finite Volume Point Dilution Method (FVPDM). It is based on an analytical solution derived from a mathematical model proposed recently to accurately model tracer injection into a well. Using a non-dimensional formulation of the analytical solution, a sensitivity analysis is performed on the concentration evolution in the injection well, according to tracer injection conditions and well-aquifer interactions. Based on this analysis, optimised field techniques and interpretation methods are proposed. The new tracer technique is easier to implement in the field than the classical point dilution method while it further allows monitoring temporal changes of the magnitude of estimated Darcy fluxes, which is not the case for the former technique. The new technique was applied to two experimental sites with contrasting objectives, geological and hydrogeological conditions, and field equipment facilities. In both cases, field tracer concentrations monitored in the injection wells were used to fit the calculated modelled concentrations by adjusting the apparent Darcy flux crossing the well screens. Modelling results are very satisfactory and indicate that the methodology is efficient and accurate, with a wide range of potential applications in different environments and experimental conditions, including the monitoring with time of changes in Darcy fluxes.     

污泥生物沥滤工艺优化和重金属分配研究

为了得到嗜酸硫细菌沥滤污泥中重金属的最佳工艺参数,对沥滤过程进行3因素4水平的正交实验研究。3种影响因素的水平设置分别为:污泥浓度35、25、15和5 g/L,单质硫投加量15、10、5和1 g/L,接种量15、10、5和3 g/L。对沥滤过程污泥中7种重金属(As、Cd、Cr、Cu、Ni、Pb和Zn)的去除率进行极差分析,提出了因素影响程度依次为单质硫投加量污泥浓度接种量,且最佳工艺条件为:污泥浓度25 g/L,单质硫投加量10 g/L,接种量为5%。采用超声波-离心方法,分步提取污泥胞外聚合物(EPS)的2种形态:松散结合态(LB)和紧密结合态(TB)。分析其中的重金属浓度,提出沥滤后重金属在污泥EPS的赋存以LB为主。