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一种从活性炭吸附等温线数据计算吸附相体积和拟饱和压力的方法。

A method for the calculation of the adsorbed phase volume and pseudo-saturation pressure from adsorption isotherm data on activated carbon.

机构信息

Department of Mechanical Engineering, National University of Singapore, Singapore117576.

出版信息

Phys Chem Chem Phys. 2011 Jul 21;13(27):12559-70. doi: 10.1039/c1cp20383e. Epub 2011 Jun 13.

Abstract

We propose a new method for evaluating the adsorbed phase volume during physisorption of several gases on activated carbon specimens. We treat the adsorbed phase as another equilibrium phase which satisfies the Gibbs equation and hence assume that the law of rectilinear diameters is applicable. Since invariably the bulk gas phase densities are known along measured isotherms, the constants of the adsorbed phase volume can be regressed from the experimental data. We take the Dubinin-Astakhov isotherm as the model for verifying our hypothesis since it is one of the few equations that accounts for adsorbed phase volume changes. In addition, the pseudo-saturation pressure in the supercritical region is calculated by letting the index of the temperature term in Dubinin's equation to be temperature dependent. Based on over 50 combinations of activated carbons and adsorbates (nitrogen, oxygen, argon, carbon dioxide, hydrocarbons and halocarbon refrigerants) it is observed that the proposed changes fit experimental data quite well.

摘要

我们提出了一种新的方法来评估几种气体在活性炭样品上物理吸附时的吸附相体积。我们将吸附相视为另一个满足吉布斯方程的平衡相,因此假设直线直径定律适用。由于在测量的等温线上始终可以知道体相气体密度,因此可以从实验数据中回归出吸附相体积常数。我们选择 Dubinin-Astakhov 等温线作为验证我们假设的模型,因为它是少数几个考虑吸附相体积变化的方程之一。此外,通过让 Dubinin 方程中的温度项指数随温度变化,计算出超临界区的伪饱和压力。基于超过 50 种活性炭和吸附剂(氮气、氧气、氩气、二氧化碳、碳氢化合物和卤代碳制冷剂)的组合,观察到所提出的变化与实验数据非常吻合。

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