MODELING OF NON-IDEAL BINARY ADSORPTION

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MAGHSOUDI HAFEZ

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Journal: JOURNAL OF SEPARATION SCIENCE AND ENGINEERING Year:2016 | Volume:8 | Issue:1 Page(s): 77-85

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Information Journal Paper

Title

MODELING OF NON-IDEAL BINARY ADSORPTION

Author(s)

MAGHSOUDI HAFEZ | Issue Writer Certificate

Keywords

NON-IDEAL ADSORPTION MODELINGQ2

REAL ADSORPTION SOLUTION THEORY (RAST)Q2

WILSON ACTIVITY COEFFICIENTSQ2

Abstract

At non-ideal multicomponent adsorption systems, adsorbed phase behavior is not well predicted by ideal adsorption solution theory (IAST). At these systems, real adsorption solution theory (RAST) can present more accurate predictions by introducing adsorbed phase activity coefficients provided that they are obtained with a suitable thermodynamic model.In this paper, RAST with Wilson equation was develop for modeling of adsorbed phase behavior. In obtaining activity coefficients of components, Gibbs–Duhem equation at only constant temperature was utilized because the spreading pressure varies at the adsorption process. According to the results of the systems investigated, it was revealed that the model reduces the average prediction errors to about 10% (in worst case) while it is more than 50% by IAST.

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APA: Copy

MAGHSOUDI, HAFEZ. (2016). MODELING OF NON-IDEAL BINARY ADSORPTION. JOURNAL OF SEPARATION SCIENCE AND ENGINEERING, 8(1), 77-85. SID. https://sid.ir/paper/356504/en

Vancouver: Copy

MAGHSOUDI HAFEZ. MODELING OF NON-IDEAL BINARY ADSORPTION. JOURNAL OF SEPARATION SCIENCE AND ENGINEERING[Internet]. 2016;8(1):77-85. Available from: https://sid.ir/paper/356504/en

IEEE: Copy

HAFEZ MAGHSOUDI, “MODELING OF NON-IDEAL BINARY ADSORPTION,” JOURNAL OF SEPARATION SCIENCE AND ENGINEERING, vol. 8, no. 1, pp. 77–85, 2016, [Online]. Available: https://sid.ir/paper/356504/en

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