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Pure and Binary Mixture Gases Adsorption Equilibria of Hydrogen/Methane/Ethylene on Activated Carbon

机译:氢气/甲烷/乙烯在活性炭上的纯净和二元混合气体吸附平衡

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摘要

Adsorption equilibria of the gases H_2,CH_4,and C_2H_4 and their binary mixtures on activated carbon (Cal-gon co.) have been measured by static volumetric method in the pressure range of 0 to 18 atm at temperatures of 293.15,303.15,and 313.15 K.From the parameters obtained from single component adsorption isotherm,multi-component adsorption equilibria could be predicted and compared with experimental data.The binary experimental data were applied to four models :extended Langmuir,extended Langmuir-Freundlich,Ideal Adsorbed Solution theory (IAST),and Vacancy Solution Model (VSM).The models were found to describe the experimental data with a reasonable accuracy.Extended L-F model predicts equilibria of mixture better than any other model.
机译:在293.15,303.15和313.15的温度下,通过静态体积法在0至18atm的压力范围内测量了H_2,CH_4和C_2H_4气体及其二元混合物在活性炭(Cal-gon co。)上的吸附平衡。根据单组分吸附等温线获得的参数,可以预测多组分吸附平衡并将其与实验数据进行比较。将二元实验数据应用于四种模型:扩展Langmuir,扩展Langmuir-Freundlich,理想吸附溶液理论(IAST) )和空缺溶液模型(VSM)。发现该模型可以合理地描述实验数据。扩展的LF模型比其他模型更能预测混合物的平衡。

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