Sorption equilibria and batch dynamics of weak acids (formic acid and monochloroacetic acid) on weak base ion exchange resins, in free base form, are studied. The reversible sorption model based on double layer theory, developed in part 1 of these studies, is extended to take into account undissociated acid species. The model fits the experimental dynamics satisfactorily over the entire range of resin conversion. Values of effective ionic pore diffusion coefficient, regressed from the observed experimental dynamics, have been satisfactorily correlated on the basis of the model. These studies reveal that the contributions of both the ionic and the undissociated molecular species are important in determining the total diffusive flux of the ac...
International audienceA bibliographic survey has highlighted the essential role of selectivity on re...
An Adsorbed Solution theory which takes into account non-idealities in both the adsorbed and the liq...
A study was undertaken on the decay of acid ion exchange resin from both a qualitative and quantitat...
Sorption equilibria and batch dynamics of strong acids (HCl and HNO3) On weak base ion exchange resi...
Differences in acid separation behaviour on weak base ion exchange resins have been investigated in ...
Higher rates of uptake of dibasic acids by weak base anion exchange resins, in comparison to those o...
A modified shrinking core model is proposed to correlate dynamics of acid sorption on weak base ion-...
Sorption behavior of phosphoric acid on the weak base resins Amberlite IRA-93 and Dowex WGR-2 is rep...
A new approach to cation-exchange kinetics views ion-exchange resin as an aggregate of uniform cylin...
Ion exchange and its industrial applications to water treatment are briefly reviewed. The emphasis h...
Adsorption equilibria Of glutaric acid and glyoxylic acid on a weakly basic ion-exchanger which has ...
The intrinsic protonation and complexation constants of an ion-exchange complexing resin, previously...
The time-evolution of Cd2+ ion sorption by Chelex 100 resin was studied in batch experiments as a fu...
The uptake equilibrium and the column dynamics of alanine by "001 x 7" resin, a strongly a...
In this work, D-II07 resin was used to remove formic acid from aqueous solution. A series of operati...
International audienceA bibliographic survey has highlighted the essential role of selectivity on re...
An Adsorbed Solution theory which takes into account non-idealities in both the adsorbed and the liq...
A study was undertaken on the decay of acid ion exchange resin from both a qualitative and quantitat...
Sorption equilibria and batch dynamics of strong acids (HCl and HNO3) On weak base ion exchange resi...
Differences in acid separation behaviour on weak base ion exchange resins have been investigated in ...
Higher rates of uptake of dibasic acids by weak base anion exchange resins, in comparison to those o...
A modified shrinking core model is proposed to correlate dynamics of acid sorption on weak base ion-...
Sorption behavior of phosphoric acid on the weak base resins Amberlite IRA-93 and Dowex WGR-2 is rep...
A new approach to cation-exchange kinetics views ion-exchange resin as an aggregate of uniform cylin...
Ion exchange and its industrial applications to water treatment are briefly reviewed. The emphasis h...
Adsorption equilibria Of glutaric acid and glyoxylic acid on a weakly basic ion-exchanger which has ...
The intrinsic protonation and complexation constants of an ion-exchange complexing resin, previously...
The time-evolution of Cd2+ ion sorption by Chelex 100 resin was studied in batch experiments as a fu...
The uptake equilibrium and the column dynamics of alanine by "001 x 7" resin, a strongly a...
In this work, D-II07 resin was used to remove formic acid from aqueous solution. A series of operati...
International audienceA bibliographic survey has highlighted the essential role of selectivity on re...
An Adsorbed Solution theory which takes into account non-idealities in both the adsorbed and the liq...
A study was undertaken on the decay of acid ion exchange resin from both a qualitative and quantitat...