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An experimental investigation of NAPL pool dissolution enhancement by flushing

机译:通过冲洗提高NAPL池溶出度的实验研究

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Experiments coupled with mathematical modeling are used to further elucidate the quantifica- tion of NAPL pool dissolution and its enhancement by water flushing. The experiments were performed using glass bead-packed column reactors with small pools of neat toluene or a toluene in dodecane mixture (toluene mole fraction, X_tol ≈ 0.02 or 0.09). Experimental quasi--steady-state toluene dissolution fluxes were determined by a mass--balance approach. The results of these experiments are used to quantity the impact of flushing on the NAPL pool dissolution flux, J, for wide ranges of two of the key controlling parameters--equilibrium concentration, C_s, and average pore water velocity, υ_x. In addition, the experimental dissolution flux data are used to evaluate predictions made using independently obtained model parameters and analytical mathematical models incorporating the two basic approaches used for mathematically describing the interphase distribution of NAPLs: the local equilibrium (LE) approach; and the mass transfer limited, or nonequilibrium (NE) approach. The data from the experiments with a neat toluene pool demon- strate the expected trend of increasing J as υ_x. increased from approximately 2 to 30 m/day. The LE model and the NE model with an average mass transfer coefficient, k_1 = 4.76 m/day, were able to describe the neat toluene pool data for υ_x < 18 m/day reasonably well. However, for υ_x > 18 m/day, the NE model with k_1 = 4.76 m/day provides a better description of the data, suggesting that the equilibrium boundary condition may become invalid for very high velocities. The experiments with the binary toluene in dodecane pools also show the expected trend of increasing J with increasing υ_x. The LE model describes the binary pool data reasonably well for the entire range of υ_x studied (approximately 0.1 to 10 m/day), and the NE model predictions with the average k_1 = 4.76 m/day determined in the neat-pool studies do not deviate significantly from the LE model in this υ_x range, although small deviations occur for > 10 m/day.
机译:结合数学模型进行的实验被用来进一步阐明NAPL池溶解的定量及其通过水冲洗的增强作用。使用玻璃珠填充柱反应器进行实验,该反应器带有少量纯净甲苯或十二烷混合物中的甲苯(甲苯摩尔分数,X_tol≈0.02或0.09)。实验准稳态甲苯溶解通量是通过质量平衡法确定的。这些实验的结果用于量化冲刷对NAPL池溶出通量J的影响,其中包括两个关键控制参数(平衡浓度C_s和平均孔隙水速度υ_x)的较宽范围。另外,实验溶解通量数据用于评估使用独立获得的模型参数和分析数学模型做出的预测,该数学模型结合了用于数学描述NAPL相间分布的两种基本方法:局部平衡(LE)方法;以及传质受限或非平衡(NE)方法。来自纯甲苯池的实验数据证明了J随υ_x增加的预期趋势。从每天约2 m增加到每天30 m。 LE模型和NE模型的平均传质系数k_1 = 4.76 m / day,能够很好地描述υ_x<18 m / day的纯甲苯库数据。但是,对于υ_x> 18 m / day,k_1 = 4.76 m / day的NE模型提供了更好的数据描述,这表明平衡边界条件对于非常高的速度可能变得无效。在十二烷池中使用二甲苯进行的实验还显示出随着υ_x的增加J的预期趋势。 LE模型在研究的整个υ_x范围内(约0.1至10 m / day)都很好地描述了二元池数据,而在净池研究中确定的平均k_1 = 4.76 m / day的NE模型预测却没有尽管在> 10 m / day的情况下会出现小的偏差,但在υ_x范围内与LE模型存在明显差异。

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