Rong Zimei, Terzyk Artur P, Gauden Piotr A, Vadgama Pankaj
IRC in Biomedical Materials, Queen Mary University of London, Mile End Road, London E1 4NS, United Kingdom.
J Colloid Interface Sci. 2007 Sep 15;313(2):449-53. doi: 10.1016/j.jcis.2007.04.070. Epub 2007 May 3.
Analytical expressions for solute adsorption kinetics within porous carbon cylindrical granules of adsorbents with a one point formula for effective diffusion coefficient determination are available based on the assumption that solute transport is the rate limiting step and that it follows Fick's Second Law. Here the first practical application of this theory is provided with an initial, estimated diffusion coefficient refined by fitting calculated kinetic adsorption curves to experimental data determined for activated carbons. In an ideal experiment, experimental error (noise) is negligible, and no data refinement is needed. However, real experimental data are always more or less noise contaminated. Where such noise is significant, a simulation method offers the best value for effective diffusion coefficient. For this specific system, surface modification, pH and temperature effects on adsorption kinetics were analysed quantitatively as a basis of determining effective diffusion coefficients through the porous structure.
基于溶质传输是速率限制步骤且遵循菲克第二定律的假设,可得到用于确定有效扩散系数的单点公式的多孔碳圆柱形吸附剂颗粒内溶质吸附动力学的解析表达式。本文首次将该理论实际应用于通过拟合计算得到的动力学吸附曲线与活性炭实测数据来优化初始估计扩散系数。在理想实验中,实验误差(噪声)可忽略不计,无需数据优化。然而,实际实验数据总会或多或少受到噪声污染。当这种噪声显著时,模拟方法可提供有效扩散系数的最佳值。对于该特定系统,定量分析了表面改性、pH值和温度对吸附动力学的影响,以此作为通过多孔结构确定有效扩散系数的基础。