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1.
环境中氡运移理论与计算方法研究   总被引:3,自引:1,他引:2  
刘庆成  程业勋  章晔 《物探与化探》1998,22(2):149-152,138
本文根据氡运移的扩散与对流理论建立了任意形状介质中氡运移方程、大地岩石、土壤中氡的运移方程和大地—大气氡交换理论模型。通过模型实验研究了介质中氡运移规律并验证所建立的氡运移的理论公式。运用大地—大气氡交换模型计算了江西临川市某住宅区空气中氡浓度,取得了初步的应用效果。  相似文献   

2.
开封市垃圾场污染物运移模拟与控制   总被引:3,自引:0,他引:3  
张艳  何江涛  李鹏  王俊杰 《地下水》2010,32(3):15-18,27
在对开封市某典型垃圾场进行野外调查的基础上,应用Visual Modflow建立了该垃圾场污染场地的水流和溶质运移耦合模型并进行数值模拟预测,预测了20年后该污染场地垃圾渗滤液污染羽运移范围、途径及方式等特点。模拟了应用防渗墙和抽水井两种方式控制地下水污染的措施和方案,并利用计算机模型对污染控制的效果进行了模拟分析。模拟结果表明,模拟初期污染羽覆盖了3个抽水井,污染羽前缘距离村庄688 m。模拟20年后污染羽已经覆盖了7个抽水井,其中浓度超标井有3口,污染羽前缘距离村庄605 m。建议在加强污染物监测的同时协助开展其他的污染控制措施,进一步控制污染羽的扩散。  相似文献   

3.
多个相关随机参数的空间变异性对溶质运移的影响   总被引:1,自引:0,他引:1       下载免费PDF全文
根据给定渗透系数、孔隙度以及吸附系数的概率分布,采用顺序高斯模拟生成相关的多参数随机场的实现,作为地下水流和溶质运移模型的输入参数,对污染物浓度进行随机分析。研究结果表明,与仅考虑渗透系数空间变异性相比,考虑相关的多参数空间变异性导致污染羽的扩散程度有显著不同。当孔隙度与渗透系数呈正相关关系时,会减少污染羽的扩散程度,反之,当孔隙度与渗透系数为负相关关系时,会加剧污染羽的扩散程度。吸附系数也是如此。在考虑吸附系数的空间变异性之后,污染羽的分布表现出拖尾现象。同时考虑渗透系数、孔隙度以及吸附系数空间变异性时,孔隙度非均质性对溶质运移的影响较吸附系数非均质性的影响更大。  相似文献   

4.
《地下水》2016,(6)
针对数值模型中结构与参数的不确定性因素,以安徽省丘陵地区一铁矿为例,通过建立地下水数值模拟模型,分别分析了结构与参数的不确定性对污染物运移结果的影响程度。分析结果表明:模型结构方面,随着数值模型的结构发生变化,污染羽中心点浓度值随厚度的增加而降低,且污染物的运移影响范围也有所缩小,当厚度增大20%时,一年末水平方向的影响范围由204 m减小至198 m,减小了近3%;参数方面,随着渗透系数的增加,污染羽中心点浓度值逐渐降低,污染羽的影响范围呈现增大的趋势,但增加的幅度较小。  相似文献   

5.
杨川  王金生 《地下水》2006,28(6):37-41
建立一维包气带溶质运移数学模型和二维潜水层溶质运移数学模型,对热电厂灰水污染物在包气带和潜水中的运移进行模拟,以下游水源地污染物浓度峰值不超过环境质量标准为依据,通过模型反复计算,得到包气带模型运行时长,即最大灰水排放时间,继而得到灰场库容.该方法可以为电厂灰场库容设计提供合理的标准,从而控制由于灰水排放所造成的潜水层污染问题.  相似文献   

6.
宋超  刘财  张宇白  鹿琪 《世界地质》2014,33(3):708-715
为研究LNAPL(轻质非水相液体)污染物在均匀含水介质中的运移规律,本文建立微元模型推导出LNAPL在均匀含水介质中的对流--弥散方程。针对不同的介质模型,对二维对流--弥散方程运用差分法进行数值模拟,求其数值解。分析LNAPL污染物的运移特征,得出在均匀介质和非均匀层状介质中运移规律:LNAPL污染物在含水介质中的运移规律遵循对流--弥散方程,介质的弥散系数是影响LNAPL污染物运移的主要因素。  相似文献   

7.
《地下水》2021,(3)
以安徽省向山垃圾填埋场作为研究区,在分析场区水文地质条件的基础上,运用GMS中的MODFLOW和MT3D模块建立地下水流概念模型、数值模型及溶质运移数值模型,并根据取样结果确定污染物因子,模拟正常状况和非正常状况下污染物在地下水环境中的污染路径、污染羽迁移状况和污染物对地下水环境可能造成的影响。研究结果表明:评价区地下水类型主要为岩浆岩类孔隙裂隙水,主要污染源位于老库区及渗滤液处理站位置。正常状况下,在模拟期范围内COD的污染羽中心浓度为1.23~3.0 mg/L,均满足地下水质量标准Ⅲ类水,对地下水环境影响十分有限;非正常状况下,污染物在地下水中沿污染中心向四周浓度逐渐减小,浓度梯度较大,污染物在含水层中沿地下水流方向呈近似椭圆形状运移,污染物在5 a、10 a、20 a与30 a后,运移距离与范围逐年增加,评价区内COD最大超标范围和最大运移距离分别可达125 423.1 m~2和640.3 m,表明事故条件下,污染物的泄露会对地下水水质造成污染。建议在填埋场的建设和运营过程中,定期监控水质的变化情况并采取相应控制措施,保证区域水生态环境安全。  相似文献   

8.
以某污染厂区为研究对象,通过野外调查并结合已有资料,利用GMS软件建立研究区域地下水流场模型和溶质运移模型,并且详细分析了地下水污染规律。研究结果表明:降雨入渗扩散方式下,污染物在地下水中的迁移速率与污染物的浓度及地下水介质密切相关。在潜水含水层中,污染物主要以垂向运移为主,并且受污染源强影响较大,污染物浓度越高,其垂向运移速率越快,污染物在水平面上的扩散速率受污染源强的影响较小;在承压含水层中,污染物沿水流方向迁移,并且呈现匀速扩散趋势。  相似文献   

9.
卫河是海河流域污染最严重的河流之一,该河如何影响附近浅层地下水的水质是长期受到重视但缺乏定量研究的关键问题。为探讨这一问题,利用Hydrus 2d模型模拟河流非饱和带氮素的迁移转化,以GMS软件中的RT3D模块模拟氮素在饱和含水层中的运移,将包气带底部淋滤出的污染物浓度定为饱和带溶质运移模型的上边界条件,首次实现了河流非饱和带饱和含水层氮素运移的联合模拟,得到河流线状污染源对浅层地下水的影响程度及范围。研究结果表明:由于吸附作用、硝化反硝化作用的存在,从河流上游到下游,包气带厚度加大,运移至含水层中的NH4-N、NO2-N浓度呈下降趋势,而NO3-N浓度则呈上升趋势。随着入渗时间的增长,进入饱和含水层中的NH4-N、NO2-N、NO3-N的浓度逐渐升高并最终保持稳定。污染的河流对浅层地下水的影响呈带状分布,污染物随入渗水流在包气带中垂直入渗;在饱和含水层中以水平运移为主,污染羽偏向地下水流动的方向,其影响距离不超过500 m。  相似文献   

10.
《地下水》2017,(3)
灰坝工程中灰水渗漏易对地下水产生污染,为预防治理地下水污染,应研究灰场污染物的运移机理,在运移工程中由于岩体裂隙的粗糙性和各向异性,渗流及溶质运移模型实际非常复杂。本文着眼于建立将粗糙裂隙岩体非连续渗流、溶质运移数学模型,应用于陡立裂隙网络岩体渗流浸润线及出漏点溶质浓度数值模拟,为定量分析灰场对地下水的影响提供理论依据。  相似文献   

11.
An approach is presented to quantify sensitivity of advective contaminant travel time to porosities of hydrogeologic units (HGUs) along the flowpaths when the porosities of different HGUs are correlated. The approach is an extension of the previous sensitivity analysis technique for independent input porosity cases. It is applicable in situations where a calibrated groundwater flow model exists, but a full contaminant transport model is not available. Three sensitivity indices are introduced based on the decomposition of covariance between the advective contaminant travel time and individual input porosities of HGUs. When the input HGU porosities are correlated, the three sensitivity indices quantify the total, intrinsic and correlated contributions from each individual HGU porosity, which should be considered in order to determine the relative importance to the uncertainty in advective contaminant travel time of the input HGU porosities contributing either independently or correlatedly. Two simple one-dimensional flow examples are presented to illustrate the applications of the approach to scenarios when each HGU has distinct porosity and situations of spatially variable porosity field. The approach is applicable to more complex multi-dimensional cases where advective contaminant travel time can be calculated based on simulated flow results from groundwater flow models.  相似文献   

12.
Consolidation of clayey contaminant barriers such as landfill liners has been postulated as a cause of early breakthrough of contaminants. In this paper we theoretically investigate this proposition. For this purpose a sophisticated one‐dimensional, large‐deformation model of coupled mechanical consolidation and solute transport is employed. This new model is a generalization of existing coupled consolidation and solute transport models described in the literature. It takes into account both non‐linearities in geometry as well as constitutive relations. The latter relate the compressibility, hydraulic conductivity and coefficient of effective diffusivity to the deformation of the soil. The model is applied to a case study of a clay liner and geomembrane system. Results obtained from numerical solution of the model equations are compared with those from various simplified models, including a ‘diffusion only’ (i.e. a rigid soil) model traditionally used in contaminant barrier design. For barriers incorporating low compressibility soils (as for many well compacted clays), there is little difference between contaminant transit (i.e. breakthrough) times predicted by the two models. However, for contaminant barriers incorporating more compressible soils, consolidation is shown to significantly accelerate transport. These results indicate the potential importance of accounting for the effects of soil consolidation and highlight the limitations of existing models when modelling solute transport through composite barriers utilizing soft soils. Based on these limited results, we suggest a possible way of taking into account soil consolidation using simplified models. Copyright © 2008 John Wiley & Sons, Ltd.  相似文献   

13.
We propose an extension of the shifted Grünwald-Letnikov method to solve fractional partial differential equations in the Caputo sense with arbitrary fractional order derivative α and with an advective term. The method uses the relation between Caputo and Riemann-Liouville definitions, the shifted Grünwald-Letnikov, and the traditional backward and forward finite difference method. The stability of the method is investigated for the implicit and explicit scheme with homogeneous boundary conditions, and a stability criterion is found for the advective-dispersive equation. An application of the method is used to solve contaminant diffusion and advective-dispersive problems. The numerical solution for the fractional diffusion and fractional advection-dispersion is compared with their respective analytical solutions for different time and space grid refinements. The diffusion simulation exhibited a good fit between the analytical and numerical solutions, with the explicit scheme going from stable to unstable as the time and space refinement changes. The fractional advection-dispersion application produced small deviations from the analytical solution. These deviations, however, are analogous to the numerical dispersions encountered in conventional finite difference solutions of the advection-dispersion equation. The new method is also compared with the traditional L2 method. Notably, an example that involves asymmetrical fractional conditions, a fractional diffusivity that depends on time, and a source term show how the methods compare. Overall, this study assesses the quality and easiness of use of the numerical method.  相似文献   

14.
Determination of necessary tracer mass, initial sample-collection time, and subsequent sample-collection frequency are the three most difficult aspects to estimate for a proposed tracer test prior to conducting the tracer test. To facilitate tracer-mass estimation, 33 mass-estimation equations have been developed over the past century. These 33 equations are reviewed here, 32 of which were evaluated using previously published tracer-test design examination parameters. Comparison of the results produced a wide range of estimated tracer mass, but no means is available by which one equation may be reasonably selected over the others. Each equation produces a simple approximation for tracer mass. Most of the equations are based primarily on estimates or measurements of discharge, transport distance, and suspected transport times. Although the basic field parameters commonly employed are appropriate for estimating tracer mass, the 33 equations are problematic in that they were all probably based on the original developers experience in a particular field area and not necessarily on measured hydraulic parameters or solute-transport theory. Suggested sampling frequencies are typically based primarily on probable transport distance, but with little regard to expected travel times. This too is problematic in that tracer sampling remains a haphazard process that tends to result in false negatives or data aliasing. Simulations from the recently developed efficient hydrologic tracer-test design methodology (EHTD) were compared with those obtained from 32 of the 33 published tracer-mass estimation equations and suggested sampling frequencies. EHTD applies functional relationships developed from hydrologic measurements in a solute-transport model to develop a preliminary tracer-breakthrough curve that has been shown to reasonably predict actual tracer-test results.  相似文献   

15.
Using the numerical model presented in the first paper of this research,1 a parametric study has been carried out in this paper to investigate the effect of several important parameters on the transient contaminant transport in infinite porous fractured media. From the related numerical results, it has been demonstrated that: (1) transmissive coefficient between the porous block and the fissured network has a significant influence on the value of the concentration but has little effect on the speed of contaminant transport; (2) porosities in the porous block and fissured network have a significant influence on the maximum value of the concentration; (3) average linear velocity of flow has a significant influence on both the concentration distribution and speed of contaminant transport; (4) dispersion coefficient of the medium affects not only the shape of the concentration versus time curve but also the peak value of the concentration.  相似文献   

16.
Hydrological tracer testing is the most reliable diagnostic technique available for the determination of basic hydraulic and geometric parameters necessary for establishing operative solute-transport processes. Tracer-test design can be difficult because of a lack of prior knowledge of the basic hydraulic and geometric parameters desired and the appropriate tracer mass to release. A new efficient hydrologic tracer-test design (EHTD) methodology has been developed to facilitate the design of tracer tests by root determination of the one-dimensional advection-dispersion equation (ADE) using a preset average tracer concentration which provides a theoretical basis for an estimate of necessary tracer mass. The method uses basic measured field parameters (e.g., discharge, distance, cross-sectional area) that are combined in functional relationships that describe solute-transport processes related to flow velocity and time of travel. These initial estimates for time of travel and velocity are then applied to a hypothetical continuous stirred tank reactor (CSTR) as an analog for the hydrological-flow system to develop initial estimates for tracer concentration, tracer mass, and axial dispersion. Application of the predicted tracer mass with the hydraulic and geometric parameters in the ADE allows for an approximation of initial sample-collection time and subsequent sample-collection frequency where a maximum of 65 samples were determined to be necessary for describing the predicted tracer-breakthrough curve (BTC). Inclusion of tracer retardation and decay cause a net increase in tracer-mass estimates so that the preset average tracer concentration will be maintained and there will be a consequent steepening of the BTC, but retardation also causes BTC spreading and a delay in tracer arrival.  相似文献   

17.
Design of a groundwater pumping and treatment system for a wood-treatment facility adjacent to the tidally influenced Fraser River estuary required the development of methodologies to account for cyclic variations in hydraulic gradients. Design of such systems must consider the effects of these cyclic fluctuations on the capture of dissolved-phase contaminants. When the period of the cyclic fluctuation is much less than the travel time of the dissolved contaminant from the source to the discharge point, the hydraulic-gradient variations resulting from these cycles can be ignored. Capture zones are then designed based on the average hydraulic gradient determined using filter techniques on continuous groundwater-level measurements. When the period of cyclic fluctuation in hydraulic gradient is near to or greater than the contaminant travel time, the resulting hydraulic-gradient variations cannot be ignored. In these instances, procedures are developed to account for these fluctuations in the capture-zone design. These include proper characterization of the groundwater regime, assessment of the average travel time and period of the cyclic fluctuations, and numerical techniques which allow accounting for the cyclic fluctuations in the design of the capture zone. Electronic Publication  相似文献   

18.
An analytical solution for one-dimensional contaminant diffusion through multi-layered media is derived regarding the change of the concentration of contaminants at the top boundary with time. The model accounts for the arbitrary initial conditions and the conditions of zero concentration and zero mass flux on the bottom boundary. The average degree of diffusion of the layered system is introduced on the basis of the solution. The results obtained by the presented analytical solutions agree well with those obtained by the numerical methods presented in the literature papers. The application of the analytical solution to the problem of landfill liner design is illustrated by considering a composite liner consisting of geomembrane and compacted clay liner. The results show that the 100-year mass flux of benzene at the bottom of the composite liner is 45 times higher than that of acetone for the same composite liner. The half-life of the contaminant has a great influence on the solute flux of benzene diffused into the underlying aquifer. Results also indicates that an additional 2.9–5.0 m of the conventional (untreated) compacted clay liner under the geomembrane is required to achieve the same level of protection as provided by 0.60 m of the Hexadecyltrimethylammonium (HDTMA)-treated compacted clay liners in conjunction with the geomembrane. Applications of the solution are also presented in the context of a contaminated two-layered media to demonstrate that different boundary and initial conditions can greatly affect the decontamination rate of the problem. The method is relatively simple to apply and can be used for performing equivalency analysis of landfill liners, preliminary design of groundwater remediation system, evaluating experimental results, and verifying more complex numerical models.  相似文献   

19.
A finite element formulation is proposed to approximate a nonlinear system of partial differential equations, composed by an elliptic subsystem for the pressure–velocity and a transport equation (convection–diffusion) for the concentration, which models the incompressible miscible displacement of one fluid by another in a rigid porous media. The pressure is approximated by the classical Galerkin method and the velocity is calculated by a post-processing technique. Then, the concentration is obtained by a Galerkin/least-squares space–time (GLS/ST) finite element method. A numerical analysis is developed for the concentration approximation. Then, stability, convergence and numerical results are presented confirming the a priori error estimates.  相似文献   

20.
李华伟  白冰  王梦恕  许韬 《岩土力学》2015,36(5):1306-1312
根据饱和多孔介质中考虑释放效应的一维渗透作用的可溶性污染物的迁移控制方程,通过Laplace变换和Fourier变换及其逆变换求得相应的通解形式。根据半无限体表面可溶性污染物点源注入情形下的基本解,通过积分方法得到半无限体表面圆形区域上作用循环浓度污染物后,在多孔介质内部污染物迁移过程的求解方法。作为一个典型算例,对渗透作用下循环浓度污染源引起的多孔介质中的迁移过程进行分析。算例表明,当污染源浓度为周期变化时,多孔介质内部污染物的浓度随时间增长由不稳定的周期变化过程逐渐过渡到稳定的循环过程,而某一深度处污染物浓度的相位则相应滞后。此时,稳定后的污染物浓度周期与污染源浓度周期相同。实际上,随多孔介质表面污染源浓度的周期变化,在靠近多孔介质表面一定深度范围内的污染物浓度在深度方向也呈增大或减小的交替变化过程。另一方面,在污染源循环变化过程中污染物不断向深处推进,而最终其影响范围限定在某一深度内。  相似文献   

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