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Pertraction of phenol in hollow-fiber membrane contactors

Authorized Users Only
2004
Authors
Trivunac, Katarina
Stevanović, S
Mitrović, M
Article (Published version)
Metadata
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Abstract
In this paper the multistage membrane pertraction (simultaneous extraction and reextraction) of phenol with linear monoalkyl cyclohexane (IMACH) as a carrier and sodium hydroxide solution as a strip, in laboratory scaled pertractors with polysulphone hollow-fiber membranes, was investigated. Two types of pertractors were used, one being "fiber-in-fiber" type, and the other "fiber-by-fiber" type, both with parallel countercurrent flow of three independent liquid streams (feed, extragent and strip). The best results were obtained with feed and strip flow rates low and equal, while the organic flow rate was four times higher. Efficiency is higher for lower phenol concentration in feed, and higher alkalinity of stripping solution. It was shown that the pertraction of phenol with IMACH as an organic carrier is an extraction step-limited process. For that reason the "fiber-by-fiber" type of pertractor offers better constructive possibilities, since it enables combining larger number of fiber...s for extraction step with a corresponding smaller number of fibers for the Stripping step, which is not possible in the case of the "fiber-in-fiber" type of pertractor.

Keywords:
phenol / linear monoalkyl cyclohexane / hollow-fiber membrane / pertraction
Source:
Desalination, 2004, 162, 1-3, 93-101
Publisher:
  • Elsevier, Amsterdam

DOI: 10.1016/S0011-9164(04)00031-1

ISSN: 0011-9164

WoS: 000220351200012

Scopus: 2-s2.0-1842763553
[ Google Scholar ]
28
22
URI
http://TechnoRep.tmf.bg.ac.rs/handle/123456789/683
Collections
  • Radovi istraživača / Researchers’ publications (TMF)
Institution/Community
Tehnološko-metalurški fakultet
TY  - JOUR
AU  - Trivunac, Katarina
AU  - Stevanović, S
AU  - Mitrović, M
PY  - 2004
UR  - http://TechnoRep.tmf.bg.ac.rs/handle/123456789/683
AB  - In this paper the multistage membrane pertraction (simultaneous extraction and reextraction) of phenol with linear monoalkyl cyclohexane (IMACH) as a carrier and sodium hydroxide solution as a strip, in laboratory scaled pertractors with polysulphone hollow-fiber membranes, was investigated. Two types of pertractors were used, one being "fiber-in-fiber" type, and the other "fiber-by-fiber" type, both with parallel countercurrent flow of three independent liquid streams (feed, extragent and strip). The best results were obtained with feed and strip flow rates low and equal, while the organic flow rate was four times higher. Efficiency is higher for lower phenol concentration in feed, and higher alkalinity of stripping solution. It was shown that the pertraction of phenol with IMACH as an organic carrier is an extraction step-limited process. For that reason the "fiber-by-fiber" type of pertractor offers better constructive possibilities, since it enables combining larger number of fibers for extraction step with a corresponding smaller number of fibers for the Stripping step, which is not possible in the case of the "fiber-in-fiber" type of pertractor.
PB  - Elsevier, Amsterdam
T2  - Desalination
T1  - Pertraction of phenol in hollow-fiber membrane contactors
EP  - 101
IS  - 1-3
SP  - 93
VL  - 162
DO  - 10.1016/S0011-9164(04)00031-1
ER  - 
@article{
author = "Trivunac, Katarina and Stevanović, S and Mitrović, M",
year = "2004",
abstract = "In this paper the multistage membrane pertraction (simultaneous extraction and reextraction) of phenol with linear monoalkyl cyclohexane (IMACH) as a carrier and sodium hydroxide solution as a strip, in laboratory scaled pertractors with polysulphone hollow-fiber membranes, was investigated. Two types of pertractors were used, one being "fiber-in-fiber" type, and the other "fiber-by-fiber" type, both with parallel countercurrent flow of three independent liquid streams (feed, extragent and strip). The best results were obtained with feed and strip flow rates low and equal, while the organic flow rate was four times higher. Efficiency is higher for lower phenol concentration in feed, and higher alkalinity of stripping solution. It was shown that the pertraction of phenol with IMACH as an organic carrier is an extraction step-limited process. For that reason the "fiber-by-fiber" type of pertractor offers better constructive possibilities, since it enables combining larger number of fibers for extraction step with a corresponding smaller number of fibers for the Stripping step, which is not possible in the case of the "fiber-in-fiber" type of pertractor.",
publisher = "Elsevier, Amsterdam",
journal = "Desalination",
title = "Pertraction of phenol in hollow-fiber membrane contactors",
pages = "101-93",
number = "1-3",
volume = "162",
doi = "10.1016/S0011-9164(04)00031-1"
}
Trivunac, K., Stevanović, S.,& Mitrović, M.. (2004). Pertraction of phenol in hollow-fiber membrane contactors. in Desalination
Elsevier, Amsterdam., 162(1-3), 93-101.
https://doi.org/10.1016/S0011-9164(04)00031-1
Trivunac K, Stevanović S, Mitrović M. Pertraction of phenol in hollow-fiber membrane contactors. in Desalination. 2004;162(1-3):93-101.
doi:10.1016/S0011-9164(04)00031-1 .
Trivunac, Katarina, Stevanović, S, Mitrović, M, "Pertraction of phenol in hollow-fiber membrane contactors" in Desalination, 162, no. 1-3 (2004):93-101,
https://doi.org/10.1016/S0011-9164(04)00031-1 . .

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