Padgett Mark C, Tick Geoffrey R, Carroll Kenneth C, Burke William R
Department of Geological Sciences, The University of Alabama, Tuscaloosa, AL 35487, United States.
Department of Geological Sciences, The University of Alabama, Tuscaloosa, AL 35487, United States.
J Contam Hydrol. 2017 Mar;198:11-23. doi: 10.1016/j.jconhyd.2017.02.001. Epub 2017 Feb 3.
The influence of chemical structure on NAPL mixture nonideality evolution, rate-limited dissolution, and contaminant mass flux was examined. The variability of measured and UNIFAC modeled NAPL activity coefficients as a function of mole fraction was compared for two NAPL mixtures containing structurally-different contaminants of concern including toluene (TOL) or trichloroethene (TCE) within a hexadecane (HEXDEC) matrix. The results showed that dissolution from the NAPL mixtures transitioned from ideality for mole fractions >0.05 to nonideality as mole fractions decreased. In particular, the TCE generally exhibited more ideal dissolution behavior except at lower mole fractions, and may indicate greater structural/polarity similarity between the two compounds. Raoult's Law and UNIFAC generally under-predicted the batch experiment results for TOL:HEXDEC mixtures especially for mole fractions ≤0.05. The dissolution rate coefficients were similar for both TOL and TCE over all mole fractions tested. Mass flux reduction (MFR) analysis showed that more efficient removal behavior occurred for TOL and TCE with larger mole fractions compared to the lower initial mole fraction mixtures (i.e. <0.2). However, compared to TOL, TCE generally exhibited more efficient removal behavior over all mole fractions tested and may have been the result of structural and molecular property differences between the compounds. Activity coefficient variability as a function of mole fraction was quantified through regression analysis and incorporated into dissolution modeling analyses for the dynamic flushing experiments. TOL elution concentrations were modeled (predicted) reasonable well using ideal and equilibrium assumptions, but the TCE elution concentrations could not be predicted using the ideal model. Rather, the dissolution modeling demonstrated that TCE elution was better described by the nonideal model whereby NAPL-phase activity coefficient varied as a function of COC mole fraction. For dynamic column flushing experiments, dissolution rate kinetics can vary significantly with changes in NAPL volume and surface area. However, under conditions whereby NAPL volume and area are not significantly altered during dissolution, mixture nonideality effects may have a greater relative control on dissolution (elution) and MFR behavior compared to kinetic rate limitations.
研究了化学结构对非水相液体(NAPL)混合物非理想性演变、限速溶解及污染物质量通量的影响。比较了两种含结构不同的目标污染物(十六烷(HEXDEC)基质中的甲苯(TOL)或三氯乙烯(TCE))的NAPL混合物实测和用UNIFAC模型预测的活度系数随摩尔分数的变化情况。结果表明,NAPL混合物的溶解从摩尔分数>0.05时的理想状态转变为摩尔分数降低时的非理想状态。特别是,TCE除在较低摩尔分数外通常表现出更理想的溶解行为,这可能表明两种化合物之间具有更大的结构/极性相似性。拉乌尔定律和UNIFAC通常低估了TOL:HEXDEC混合物的批次实验结果,尤其是对于摩尔分数≤0.05的情况。在所有测试的摩尔分数范围内,TOL和TCE的溶解速率系数相似。质量通量降低(MFR)分析表明,与较低初始摩尔分数混合物(即<0.2)相比,较高摩尔分数的TOL和TCE具有更高效的去除行为。然而,与TOL相比,TCE在所有测试的摩尔分数范围内通常表现出更高效的去除行为,这可能是化合物之间结构和分子性质差异的结果。通过回归分析量化了活度系数随摩尔分数的变化,并将其纳入动态冲洗实验的溶解建模分析中。使用理想和平衡假设对TOL洗脱浓度进行建模(预测)效果较好,但使用理想模型无法预测TCE洗脱浓度。相反,溶解建模表明,非理想模型能更好地描述TCE洗脱,即NAPL相活度系数随有机碳(COC)摩尔分数变化。对于动态柱冲洗实验,溶解速率动力学可能会随NAPL体积和表面积的变化而显著变化。然而,在溶解过程中NAPL体积和面积无显著变化的条件下,与动力学速率限制相比,混合物非理想性效应可能对溶解(洗脱)和MFR行为具有更大的相对控制作用。