THERMODYNAMIC STUDY ON ADSORPTION OF AROMATIC SULFONIC ACIDS ONTO MACROPOROUS WEAK BASE ANION EXCHANGER FROM AQUEOUS SOLUTIONS
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THERMODYNAMIC STUDY ON ADSORPTION OF AROMATIC SULFONIC ACIDS ONTO MACROPOROUS WEAK BASE ANION EXCHANGER FROM AQUEOUS SOLUTIONS
Vol. 22, Issue 6, Pages: 535-542(2004)
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Published:20 December 2004
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Chao Long, Quan-xing Zhang, Ai-min Li, et al. THERMODYNAMIC STUDY ON ADSORPTION OF AROMATIC SULFONIC ACIDS ONTO MACROPOROUS WEAK BASE ANION EXCHANGER FROM AQUEOUS SOLUTIONS[J]. 2004, 22(6): 535-542.
DOI:
Chao Long, Quan-xing Zhang, Ai-min Li, et al. THERMODYNAMIC STUDY ON ADSORPTION OF AROMATIC SULFONIC ACIDS ONTO MACROPOROUS WEAK BASE ANION EXCHANGER FROM AQUEOUS SOLUTIONS[J]. 2004, 22(6): 535-542.DOI:
THERMODYNAMIC STUDY ON ADSORPTION OF AROMATIC SULFONIC ACIDS ONTO MACROPOROUS WEAK BASE ANION EXCHANGER FROM AQUEOUS SOLUTIONS
The adsorption equilibrium isotherms of three aromatic sulfonic acid compounds
2-naphthalenesulfonic acid
p-toluenesulfonic acid and p-chlorobenzenesulfonic acid
from aqueous solutions by macroporous weak base anion exchanger within the temperature range of 293 K?313 K were obtained. Several isotherm equations were correlated with the equilibrium data
and the experimental data was found to fit the three-parameter Redlich-Peterson equation best within the entire range of concentrations. The study showed that the hydrophobicity of solute has distinct influence on adsorption capacity of the anion exchanger for the aromatic sulfonic acid. Moreover
estimations of the isosteric enthalpy
free energy
and entropy change of adsorption were also reported. The positive isosteric enthalpy and entropy change for adsorption indicate an endothermic and entropy driven process in the present study.
Abstract
The adsorption equilibrium isotherms of three aromatic sulfonic acid compounds
2-naphthalenesulfonic acid
p-toluenesulfonic acid and p-chlorobenzenesulfonic acid
from aqueous solutions by macroporous weak base anion exchanger within the temperature range of 293 K?313 K were obtained. Several isotherm equations were correlated with the equilibrium data
and the experimental data was found to fit the three-parameter Redlich-Peterson equation best within the entire range of concentrations. The study showed that the hydrophobicity of solute has distinct influence on adsorption capacity of the anion exchanger for the aromatic sulfonic acid. Moreover
estimations of the isosteric enthalpy
free energy
and entropy change of adsorption were also reported. The positive isosteric enthalpy and entropy change for adsorption indicate an endothermic and entropy driven process in the present study.
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