Review Article

Status of the Reactive Extraction as a Method of Separation

Table 2

Extractant/diluent system for the separation of carboxylic acids by reactive extraction: kinetic studies.

SL numberCarboxylic acidExtractantDiluentParametersFindingsReferences

1Penicillin GAmberlite LA-2KeroseneAgitation speed, interfacial area between two immiscible solutions, pH of aqueous phase, initial carrier, and penicillin G concentrationA rate equation for the mass transfer was proposed with the forward and backward rate constants as = 1.64 L3 mol−2 s−1 and = 6.56 × 10−5 L s−1, respectively[49]

2CitricTOAiso-decanol and n-paraffinConcentrations of acid and amine and speed of agitationFormal elementary kinetic model proposed and reaction kinetics evaluated[50]

3Penicillin GAmberlite LA-2Kerosene and n-butyl acetateAqueous and organic phase compositions, pH, and temperatureThe fractional resistances of aqueous layer diffusion, interfacial chemical reaction, and organic layer diffusion were quantitatively determined[51]

4TartaricTIOAiso-decanol, and keroseneConcentrations of acid, amine, and iso-decanolModified Langmuir isotherm was proposed and kinetic parameters interpreted by a formal elementary kinetic model[52]

5LacticAliquat 336Oleyl alcoholInitial lactate and extractant concentrations in extraction, initial chloride, and extractant-lactate complex concentrations in strippingExtraction and stripping kinetics were investigated, diffusion through the organic-phase film was determined as the rate-determining step[53]

6Phenyl aceticAlamine 336Kerosene and MIBKAcid and amine concentration, volume ratio of phases, and stirrer speedIntrinsic kinetics were described; the reaction found to be zero order in Alamine 336 and first order in acid with a rate constant of 0.9 s−1[54]

7Penicillin GAmberlite LA-2KeroseneAcid and amine concentration, and pHDispersed liquid-liquid extraction system proposed; Danckwert and Biot nos used to determine rate step[55]