Enzyme mass-transfer coefficient in aqueous two-phase systems using static mixer extraction column
被引:0
作者:
K. Rostami
论文数: 0引用数: 0
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机构:No. 71 Forsat Street,
K. Rostami
M. Alamshahi
论文数: 0引用数: 0
h-index: 0
机构:No. 71 Forsat Street,
M. Alamshahi
机构:
[1] No. 71 Forsat Street,
[2] Biotechnology Center,undefined
[3] Iranian Research Organization for Science and Technology,undefined
[4] Tehran-15819,undefined
[5] Iran,undefined
来源:
Bioprocess and Biosystems Engineering
|
2002年
/
25卷
关键词:
Enzyme mass transfer Static mixer Aqueous two-phase system;
D O I:
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摘要:
Recent technical advances in aqueous two-phase systems (ATPS) have made this a sound technique for the extraction of biomacromolecules. The extraction of α-amylase was investigated using aqueous two-phase systems formed by sodium sulphate–polyethylene glycol (PEG) in water in a 47-mm inner diameter spray column packed with three types of static mixers. The effects of dispersed-phase flow rate, phase composition, column height and diameter were studied. The extraction column was operated in a semi-batch manner. It was found that the hold-up and volumetric mass transfer coefficients increased with an increase in dispersed (PEG-rich) phase velocity and decreased with increasing phase composition. Empirical correlations were developed for fractional dispersed-phase hold-up and volumetric mass transfer coefficients.