Abstract
A semi-empirical model has been developed in ultrafiltration of huanggi (Radix astragulus) extracts. Three major fouling resistances were quantified with transmembrane pressure (TMP) ranged from 0.4 to 0.8 bar and process time lasted for 120 min. Adsorption grew fast at the initial 15 min and its contribution was more significant at 0.4 bar, nearly 50%. Pore blocking almost kept the same values of 1.28, 1.84, and 2.39 at pressures of 0.4, 0.6, and 0.8 bar, respectively. Cake layer grew linearly at 0.4 bar but it increased rapidly as the TMP arose. With the TMP increased, the contribution of cake layer became more significant, almost 75% at 0.8 bar which was triple of that at 0.4 bar. Prediction of flux decline fitted quite well with the experimental data, all within 5% errors. It demonstrates that adsorption, pore blocking, and cake layer are the main mechanisms for membrane fouling during the process.
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Rai P, Rai C, Majumdar GC, DasGupta S, De S. Resistance in series model for ultrafiltration of mosambi (Citrus sinensis (L.) Osbeck) juice in a stirred continuous mode. J. Membrane Sci. 283: 116–122 (2006)
Bowen WR, Jenner F. Theoretical descriptions of membrane filtration of colloids and fine particles an assessment and review. Adv. Colloid Interfac. 56: 141–200 (1995)
Fane AG, Fell CJD, Waters AG. Ultrafiltration of protein solutions through partially permeable membranes-the effect of adsorption and solution environment. J. Membrane Sci. 16: 211–224 (1983)
Ulbricht M, Ansorge W, Danielzik I, König M, Schuster O. Fouling in microfiltration of wine: The influence of the membrane polymer on adsorption of polyphenols and polysaccharides. Sep. Purif. Technol. 68: 335–342 (2009)
Belfort G, Davis RH, Zydney AL. The behavior of suspensions and macromolecular solutions in crossflow microfiltration. J. Membrane Sci. 96: 1–58 (1994)
Song L. Flux decline in crossflow microfiltration and ultrafiltration: Mechanisms and modeling of membrane fouling. J. Membrane Sci. 139: 183–200 (1998)
Hong SK, Faibish RS, Elimelech M. Kinetics of permeate flux decline in crossflow membrane filtration of colloidal suspensions. J. Colloid Interfac. Sci. 196: 267–277 (1997)
Kim J, DiGiano FA. Fouling models for low-pressure membrane systems. Sep. Purif. Technol. 68: 293–304 (2009)
Le-Clech P, Chen V, Fane TAG. Fouling in membrane bioreactors used in wastewater treatment. J. Membrane Sci. 284: 17–53 (2006)
Ho CC, Zydney AL. A combined pore blockage and cake filtration model for protein fouling during microfiltration. J. Colloid Interfac. Sci. 232: 389–399 (2000)
Yuan W, Kocic A, Zydney AL. Analysis of humic acid fouling during microfiltration using a pore blockage-cake filtration model. J. Membrane Sci. 198: 51–62 (2002)
Purkait MK, DasGupta S, De S. Resistance in series model for micellar enhanced ultrafiltration of eosin dye. J. Colloid Interfac. Sci. 270: 496–506 (2004)
Choi H, Zhang K, Dionysiou DD, Oerther DB, Sorial GA. Influence of cross-flow velocity on membrane performance during filtration of biological suspension. J. Membrane Sci. 248: 189–199 (2005)
Koh LC, Ahn WY, Clark MM. Selective adsorption of natural organic foulants by polysulfone colloids: Effect on ultrafiltration fouling. J. Membrane Sci. 281: 472–479 (2006)
Mohammadi T, Kohpeyma A, Sadrzadeh M. Mathematical modeling of flux decline in ultrafiltrtion. Desalination 184: 367–375 (2005)
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Cai, M., Wang, S. & Liang, H. Modeling and fouling mechanisms for ultrafiltration of Huanggi (Radix astragalus) extracts. Food Sci Biotechnol 22, 407–412 (2013). https://doi.org/10.1007/s10068-013-0094-9
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DOI: https://doi.org/10.1007/s10068-013-0094-9