dc.contributor.author |
Boukouvalas, C |
en |
dc.contributor.author |
Louli, V |
en |
dc.contributor.author |
Magoulas, K |
en |
dc.date.accessioned |
2014-03-01T01:16:11Z |
|
dc.date.available |
2014-03-01T01:16:11Z |
|
dc.date.issued |
2001 |
en |
dc.identifier.issn |
0149-6395 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/13968 |
|
dc.subject |
Co-solvent |
en |
dc.subject |
EoS/GE model |
en |
dc.subject |
Flow rate |
en |
dc.subject |
Overall volumetric mass transfer coefficients |
en |
dc.subject |
Pressure |
en |
dc.subject |
Supercritical fluid extraction |
en |
dc.subject.classification |
Chemistry, Multidisciplinary |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Equations of state of liquids |
en |
dc.subject.other |
Extraction |
en |
dc.subject.other |
Flow patterns |
en |
dc.subject.other |
Gibbs free energy |
en |
dc.subject.other |
Phenols |
en |
dc.subject.other |
Pressure effects |
en |
dc.subject.other |
Solutions |
en |
dc.subject.other |
Thermodynamic models |
en |
dc.subject.other |
Supercritical fluids |
en |
dc.subject.other |
phenol |
en |
dc.subject.other |
aqueous solution |
en |
dc.subject.other |
liquid-liquid extraction |
en |
dc.subject.other |
phenol |
en |
dc.subject.other |
pollutant removal |
en |
dc.subject.other |
supercritical fluid |
en |
dc.subject.other |
aqueous solution |
en |
dc.subject.other |
article |
en |
dc.subject.other |
chemical analysis |
en |
dc.subject.other |
correlation function |
en |
dc.subject.other |
flow rate |
en |
dc.subject.other |
mathematical analysis |
en |
dc.subject.other |
pollutant |
en |
dc.subject.other |
pollution control |
en |
dc.subject.other |
pressure |
en |
dc.subject.other |
supercritical fluid extraction |
en |
dc.subject.other |
thermodynamics |
en |
dc.subject.other |
volumetry |
en |
dc.title |
Bench-scale application of supercritical fluid extraction for the removal of phenol from aqueous solution |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1081/SS-100105918 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1081/SS-100105918 |
en |
heal.language |
English |
en |
heal.publicationDate |
2001 |
en |
heal.abstract |
The supercritical fluid extraction of phenol, a common pollutant, from aqueous solutions is performed in a bench-scale extraction apparatus through the use of supercritical CO2 at 150 bar and 45 degreesC. The obtained results are satisfactory, and the influence of pressure and flow rate of supercritical CO2, as well as the co-solvent effect, are examined. Finally, the LCVM (Linear Combination of Vidal and Michelsen) mixing rules model, an EoS/G(E) (Equation of State/Gibbs free energy) one, thermodynamic model with new interaction parameters, combined with a simple mathematical one, is used successfully for the correlation of the experimental results by adjusting the overall volumetric mass transfer coefficients of the process. |
en |
heal.publisher |
MARCEL DEKKER INC |
en |
heal.journalName |
Separation Science and Technology |
en |
dc.identifier.doi |
10.1081/SS-100105918 |
en |
dc.identifier.isi |
ISI:000171018800010 |
en |
dc.identifier.volume |
36 |
en |
dc.identifier.issue |
10 |
en |
dc.identifier.spage |
2279 |
en |
dc.identifier.epage |
2291 |
en |