Membrane filtration with reversible adsorption: The effect of transmembrane pressure, feed flow rate, and the geometry of hollow fiber filters on their performance
Document Type
Article
Publication Date
7-1-2005
Abstract
The effect of transmembrane pressure, feed flow rate, and the geometry of hollow-fiber filters on their performance is studied for depth membrane filtration with reversible adsorption. Mathematical models for rectangular and radial filters are used to find the maximal operation times with a filter retention of not less than 0.9 at constant product (permeate plus filtrate) flow rates for the treatment of a latex suspension in continuous-flow and batch operations. It is shown that the maximal operation time and, hence, product volume is achieved when the feed flow rate approaches the initial permeate flow rate. It is also found that several filters with a lower initial permeate flow rate allow one to achieve a much longer operation time than one filter with the same total initial permeate flow rate. © 2005 MAIK "Nauka/ Interperiodica".
Identifier
24144436214 (Scopus)
Publication Title
Theoretical Foundations of Chemical Engineering
External Full Text Location
https://doi.org/10.1007/s11236-005-0094-4
ISSN
00405795
First Page
402
Last Page
406
Issue
4
Volume
39
Grant
04-02-17281
Fund Ref
Russian Foundation for Basic Research
Recommended Citation
Polyakov, Yu S. and Kazenin, D. A., "Membrane filtration with reversible adsorption: The effect of transmembrane pressure, feed flow rate, and the geometry of hollow fiber filters on their performance" (2005). Faculty Publications. 19643.
https://digitalcommons.njit.edu/fac_pubs/19643
