Multicomponent adsorption equilibria of organic components from aqueous solutions on activated carbons were measured and the applicability of the ideal adsorbed solution (IAS) theory was tested. Systematic deviations between experiments and theory were observed. Absorbed phase activity coefficients which account for these deviations proved to be thermodynamically inconsistent. However, the calculation of spreading pressure in the IAS theory requires extrapolation of single solute isotherms to zero concentration. A correction of extrapolation errors was determined by fitting binary equilibrium data to the IAS theory. For a mixture of N components, N-1 constants have to be obtained from binary mixtures of N-1 components with a reference component. This work is pertinent to the treatment of industrial waste-waters and for the purification of the effluents.
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Univ Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, MalaysiaUniv Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, Malaysia
Ismail, Marhaina
Bustam, Mohamad Azmi
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Univ Teknol PETRONAS, Ctr Res Ion Liquids CORIL, Bandar Seri Iskandar 32610, Perak, MalaysiaUniv Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, Malaysia
Bustam, Mohamad Azmi
Kari, Nor Ernie Fatriyah
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Univ Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, MalaysiaUniv Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, Malaysia
Kari, Nor Ernie Fatriyah
Yeong, Yin Fong
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Univ Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, MalaysiaUniv Teknol PETRONAS, Carbon Dioxide Res Ctr CO2RES, Bandar Seri Iskandar 32610, Perak, Malaysia