Premium
Laboratory‐ and pilot plant‐scale study on the dehydration of cyclohexane by pervaporation
Author(s) -
Ortiz Inmaculada,
Urtiaga Ane,
Ibáñez Raquel,
Gómez Pedro,
Gorri Daniel
Publication year - 2006
Publication title -
journal of chemical technology and biotechnology
Language(s) - English
Resource type - Journals
SCImago Journal Rank - 0.64
H-Index - 117
eISSN - 1097-4660
pISSN - 0268-2575
DOI - 10.1002/jctb.1356
Subject(s) - pervaporation , cyclohexane , membrane , dehydration , mass transfer , pilot plant , mass transfer coefficient , chemical engineering , chemistry , solvent , materials science , chromatography , permeation , organic chemistry , engineering , biochemistry
In this work, pervaporation is applied for the dehydration of industrial cyclohexane, used as a solvent and reaction medium in the manufacture of synthetic rubbers. Working with initial concentrations of water in cyclohexane within the range of 0.090–0.110 kg m −3 , an experimental study was performed (i) in the laboratory, using a radial cell with a membrane area of 0.0178 m 2 ; and (ii) in a pilot plant located at the industrial site, with a plate‐and‐frame membrane module and a total membrane area of 3 m2. In both cases, the same pervaporation membrane, with a preferential flux of water, was used. The mass transfer coefficient was determined, together with its dependence on the hydrodynamic regime. The higher hydraulic resistance of the plate‐and‐frame module generated a pressure decrease that limited the feed velocity, thus increasing the mass transfer resistance of the pervaporation process in comparison with the bench‐scale system. Copyright © 2005 Society of Chemical Industry
Accelerating Research
Robert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom
Address
John Eccles HouseRobert Robinson Avenue,
Oxford Science Park, Oxford
OX4 4GP, United Kingdom