1998
DOI: 10.1002/aic.690440520
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Adsorption of organic acids on weakly basic ion exchanger: Equilibria for binary systems

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Cited by 24 publications
(6 citation statements)
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“…(4) with a selectivity coefficient was compared with the experimental isotherm by Eq. (10). The isotherms of benzoate ion and propionate ion ion-exchange onto the 16 kinds of resin listed in Tables 1 and 2 were investigated, and the parameters k and n and the selectivity coefficients S A Cl were obtained, as shown in Table 4, where the parameter k, which became less than 0.01 was denoted as <0.01, and Q AH was neglected in calculation because of very few.…”
Section: Confirmation For Application Of the Theoretical Equationmentioning
confidence: 99%
See 1 more Smart Citation
“…(4) with a selectivity coefficient was compared with the experimental isotherm by Eq. (10). The isotherms of benzoate ion and propionate ion ion-exchange onto the 16 kinds of resin listed in Tables 1 and 2 were investigated, and the parameters k and n and the selectivity coefficients S A Cl were obtained, as shown in Table 4, where the parameter k, which became less than 0.01 was denoted as <0.01, and Q AH was neglected in calculation because of very few.…”
Section: Confirmation For Application Of the Theoretical Equationmentioning
confidence: 99%
“…However, there are few fundamental researches on adsorption of organic compounds by anionexchange resins [9][10][11][12][13]; the information on the adsorption characteristics of organic acids onto anion-exchange resins is not sufficient.…”
Section: Introductionmentioning
confidence: 99%
“…The separating of amino and organic acids in single or binary systems has been already reported by one of the authors using adsorption/ion exchange technology. [30][31][32][33][34] However, separation of multicomponent organic compounds will be reported in the subsequent stages of this research.…”
Section: Materials Balancementioning
confidence: 99%
“…This technique can be employed at a large scale in the recovery and purification of biomolecules and has been used for citric acid recovery from fermentation broth by ion-exchange resins ( Scheme 1 , path c). Several resins are employed in this process such as macroporous resins Amberlite XAD-4 and XAD-16, 21 commercial weakly basic resin Diaion WA30, 22 Amberlite IRA-67, 23 and tailor-made tertiary PVP resin. 24 Although high selectivity and efficiency were achieved by the adsorption using ion-exchange resins, the resins need to be regenerated and replaced, producing a lot of solid and liquid waste.…”
Section: Introductionmentioning
confidence: 99%