TY - JOUR
T1 - Reactive extraction of amino acids and dipeptides using an extra-flow hollow-fiber module
AU - Hossain, Md Monwar
N1 - Funding Information:
The financial assistance of the Foundation for Research, Science and Technology (FRST), New Zealand, in the Industrial Separation Technologies Programme CO8515-1 is gratefully acknowledged. The author would like to thank the Analytical Science Team of Industrial Research Limited, Lower Hutt, New Zealand, for the analysis of the hydrolysate samples.
PY - 2005/4
Y1 - 2005/4
N2 - The extraction of amino acids (tryptophan (Trp), phenylalanine (Phe) and dipeptides (tryptophan-leucine (Trp-Leu), phenylalanine-leucine (Phe-Leu)) is examined by passing a "feed" solution (an aqueous solution containing any of the target solutes) through the fiber-side of an extra-flow hollow-fiber membrane module (HFMM). The membrane module (2.5 cm diameter × 20 cm long) has a shell-and-tube configuration and allows flow of two solutions in the fiber and shell sides. The extraction solution contained an ionic carrier, Aerosol OT (AOT), dissolved in a solvent, oleyl alcohol. The feed and organic solutions were circulated on the fiber side and shell side, respectively. The target solute (any of the amino acids or peptides) diffuses to the interface, forms a complex with the carrier; the carrier-solute complex is transported to the shell side, where it can be recovered. A mathematical model that includes the equilibrium distribution at the interfaces and the convective flow in the module is presented. A straightforward use of the experimental data has been shown to be able to calculate the overall mass transfer coefficient of the extraction process. The value of the overall mass transfer coefficient is similar to those in the literature and has been found to be significantly affected by the solute type and feed solution pH.
AB - The extraction of amino acids (tryptophan (Trp), phenylalanine (Phe) and dipeptides (tryptophan-leucine (Trp-Leu), phenylalanine-leucine (Phe-Leu)) is examined by passing a "feed" solution (an aqueous solution containing any of the target solutes) through the fiber-side of an extra-flow hollow-fiber membrane module (HFMM). The membrane module (2.5 cm diameter × 20 cm long) has a shell-and-tube configuration and allows flow of two solutions in the fiber and shell sides. The extraction solution contained an ionic carrier, Aerosol OT (AOT), dissolved in a solvent, oleyl alcohol. The feed and organic solutions were circulated on the fiber side and shell side, respectively. The target solute (any of the amino acids or peptides) diffuses to the interface, forms a complex with the carrier; the carrier-solute complex is transported to the shell side, where it can be recovered. A mathematical model that includes the equilibrium distribution at the interfaces and the convective flow in the module is presented. A straightforward use of the experimental data has been shown to be able to calculate the overall mass transfer coefficient of the extraction process. The value of the overall mass transfer coefficient is similar to those in the literature and has been found to be significantly affected by the solute type and feed solution pH.
KW - Amino acids
KW - Dipeptides
KW - Hollow-fiber module
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U2 - 10.1016/j.seppur.2004.08.001
DO - 10.1016/j.seppur.2004.08.001
M3 - Article
AN - SCOPUS:14044259959
SN - 1383-5866
VL - 42
SP - 227
EP - 236
JO - Separation and Purification Technology
JF - Separation and Purification Technology
IS - 3
ER -