Rights statement: This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see https://pubs.acs.org/doi/10.1021/acs.jced.9b00376
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Research output: Contribution to Journal/Magazine › Journal article › peer-review
Research output: Contribution to Journal/Magazine › Journal article › peer-review
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TY - JOUR
T1 - Liquid-liquid phase equilibria of aqueous biphasic systems based on glycerol formal
T2 - Application on tetracycline recovery from water
AU - Praikaew, W.
AU - Kiatkittipong, W.
AU - Kiatkittipong, K.
AU - Assabumrungrat, S.
AU - Aiouache, F.
AU - Najdanovic-Visak, V.
N1 - This document is the Accepted Manuscript version of a Published Work that appeared in final form in Journal of Chemical and Engineering Data, copyright © American Chemical Society after peer review and technical editing by the publisher. To access the final edited and published work see https://pubs.acs.org/doi/10.1021/acs.jced.9b00376
PY - 2019/11/1
Y1 - 2019/11/1
N2 - Biopharmaceuticals are commonly present in relatively low concentrations in aqueous solutions, making their detection and purification detrimental. In this work, we used novel aqueous biphasic systems based on glycerol formal (GF) to extract an important antibiotic - tetracycline. We report cloud points (solubility curve) and tie-lines for three ternary systems, containing GF, water, and inorganic salt (either K 3PO 4, K 2HPO 4, or K 2CO 3) at constant temperature of 298 K and at 0.1 MPa. The tie-line data of these ternary systems were correlated using the nonrandom two-liquid model, and binary interaction parameters of activity coefficients were estimated. The experimental and correlated tie-line data were compared in terms of average root-mean-square deviation and showed satisfactory agreements. The partition coefficients of tetracycline between two phases were measured, and corresponding extraction efficiencies were calculated. The maximum value of partition coefficient was 1551 for the system containing K 3PO 4, followed by values of 1145 and 927 for systems containing K 2CO 3 and K 2HPO 4, respectively. The calculated extraction efficiencies were very high - greater than 98.8%, demonstrating high potential for using aqueous biphasic systems based on GF for separation and purification processes.
AB - Biopharmaceuticals are commonly present in relatively low concentrations in aqueous solutions, making their detection and purification detrimental. In this work, we used novel aqueous biphasic systems based on glycerol formal (GF) to extract an important antibiotic - tetracycline. We report cloud points (solubility curve) and tie-lines for three ternary systems, containing GF, water, and inorganic salt (either K 3PO 4, K 2HPO 4, or K 2CO 3) at constant temperature of 298 K and at 0.1 MPa. The tie-line data of these ternary systems were correlated using the nonrandom two-liquid model, and binary interaction parameters of activity coefficients were estimated. The experimental and correlated tie-line data were compared in terms of average root-mean-square deviation and showed satisfactory agreements. The partition coefficients of tetracycline between two phases were measured, and corresponding extraction efficiencies were calculated. The maximum value of partition coefficient was 1551 for the system containing K 3PO 4, followed by values of 1145 and 927 for systems containing K 2CO 3 and K 2HPO 4, respectively. The calculated extraction efficiencies were very high - greater than 98.8%, demonstrating high potential for using aqueous biphasic systems based on GF for separation and purification processes.
KW - Efficiency
KW - Glycerol
KW - Liquids
KW - Phase equilibria
KW - Potash
KW - Purification
KW - Solvent extraction
KW - Aqueous biphasic system
KW - Binary interaction parameter
KW - Extraction efficiencies
KW - Liquid-liquid phase equilibria
KW - Nonrandom two-liquid model
KW - Partition coefficient
KW - Root mean square deviations
KW - Separation and purification
KW - Ternary systems
U2 - 10.1021/acs.jced.9b00376
DO - 10.1021/acs.jced.9b00376
M3 - Journal article
VL - 64
SP - 4856
EP - 4862
JO - Journal of Chemical and Engineering Data
JF - Journal of Chemical and Engineering Data
SN - 0021-9568
IS - 11
ER -