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Modelling solute transport in porous media with spatially variable multiple reaction processes.

机译:使用空间可变的多个反应过程模拟多孔介质中的溶质运移。

摘要

In this dissertation, a new numerical method is developed for the simulation of nonideal solute transport in porous media, and a first order semi-analytical solution is derived for solute transport in porous media with spatially variable multiple reaction processes. The Laplace transform is used to eliminate the time dependency and the transformed transport equations are solved both numerically and analytically. The transport solution is ultimately recovered by an efficient quotient-difference inversion algorithm. By introducing complex-valued artificial dispersion in the weighting functions, characteristics of transport solutions have been successfully addressed. The optimum of the complex-valued artificial dispersion has been derived for one dimensional problems. In multidimensional cases, the streamline upwind scheme is modified by adding complex-valued artificial dispersion along the streamline. Within this numerical scheme, the grid orientation problems have been successfully treated. The limitations on the cell Peclet number and on the Courant number were greatly relaxed. Both one dimensional and two dimensional numerical examples are used to illustrate applications of this technique. The analysis has been made for solute transport in systems with spatially variable multiple reaction processes. Specific reaction processes include reversible sorption and irreversible transformations (such as radioactive decay, hydrolysis reactions with fixed pH, and biodegradation). With the assumptions of solute transport in a system with constant hydraulic conductivity and hydrodynamic dispersion and spatially variable multiple reaction processes, a first-order semi-analytical solution is derived for an arbitrary autocovariance function, which characterizes the spatial variation of the multiple reaction processes. Results indicate that spatial variation of the transformation constants for the solution phase and the sorbed phase decreases the global rate of mass loss and enhances solute transport. If the transformation constant for the sorbed phase is spatially uniform but not zero, a similar effect is observed when there is spatial variation of the equilibrium sorption coefficient. The global rate of mass loss and apparent retardation are decreased when the spatial variability of the sorbed-phase transformation constant is positively correlated with the spatial variability of the equilibrium sorption coefficient, and increased for a negative correlation. Spatial variation of the sorption rate coefficient had minimal effect on transport.
机译:本文为模拟非理想溶质在多孔介质中的运移提供了一种新的数值方法,并导出了具有空间可变多重反应过程的多孔介质中溶质运移的一阶半解析解。使用拉普拉斯(Laplace)变换消除时间依赖性,并在数值和解析上求解变换后的输运方程。最终通过有效的商差反演算法恢复运输解决方案。通过在加权函数中引入复数值人工分散,可以成功解决运输解决方案的特征。对于一维问题,已经得出了复数值人工色散的最佳值。在多维情况下,通过沿流线添加复值人工离差来修改流线上风方案。在此数值方案内,网格定向问题已得到成功解决。对单元Peclet编号和Courant编号的限制已大大放松。一维和二维数值示例均用于说明该技术的应用。已经对具有空间可变的多个反应过程的系统中的溶质运输进行了分析。具体的反应过程包括可逆的吸附和不可逆的转化(例如放射性衰变,固定pH值的水解反应和生物降解)。假设在具有恒定的水力传导率和流体动力分散以及空间可变的多个反应过程的系统中进行溶质运移,则针对任意自协方差函数推导了一阶半解析解,该解表征了多个反应过程的空间变化。结果表明,溶液相和吸附相转化常数的空间变化降低了整体质量损失率,并提高了溶质运移。如果吸附相的转化常数在空间上均匀但不为零,则当平衡吸附系数存在空间变化时,会观察到类似的效果。当吸附相变常数的空间变异性与平衡吸附系数的空间变异性正相关时,整体质量损失率和表观延迟降低,而对于负相关性则增加。吸附速率系数的空间变化对运输的影响最小。

著录项

  • 作者

    Xu Linlin.;

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  • 年度 1995
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  • 原文格式 PDF
  • 正文语种 en
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