dc.contributor.author |
Vrachnos, A |
en |
dc.contributor.author |
Voutsas, E |
en |
dc.contributor.author |
Magoulas, K |
en |
dc.contributor.author |
Lygeros, A |
en |
dc.date.accessioned |
2014-03-01T01:21:38Z |
|
dc.date.available |
2014-03-01T01:21:38Z |
|
dc.date.issued |
2004 |
en |
dc.identifier.issn |
0888-5885 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/16289 |
|
dc.subject |
Thermodynamics |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Data acquisition |
en |
dc.subject.other |
Electrolytes |
en |
dc.subject.other |
Phase equilibria |
en |
dc.subject.other |
Regression analysis |
en |
dc.subject.other |
Thermal effects |
en |
dc.subject.other |
Acid gas-MDEA-water systems |
en |
dc.subject.other |
Electrolyte-LCVM model |
en |
dc.subject.other |
Thermodynamics |
en |
dc.subject.other |
electrolyte |
en |
dc.subject.other |
ethanolamine |
en |
dc.subject.other |
water |
en |
dc.subject.other |
vapor-liquid equilibrium |
en |
dc.subject.other |
accuracy |
en |
dc.subject.other |
article |
en |
dc.subject.other |
concentration (parameters) |
en |
dc.subject.other |
gas analysis |
en |
dc.subject.other |
model |
en |
dc.subject.other |
pressure |
en |
dc.subject.other |
thermodynamics |
en |
dc.subject.other |
vapor |
en |
dc.subject.other |
water supply |
en |
dc.title |
Thermodynamics of acid gas-MDEA-water systems |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1021/ie030769v |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1021/ie030769v |
en |
heal.language |
English |
en |
heal.publicationDate |
2004 |
en |
heal.abstract |
A thermodynamic framework for representing chemical and vapor-liquid equilibria in acid gas-MDEA-water systems has been developed. The vapor-liquid equilibrium is calculated through a new EoS/G(E) model called the electrolyte-LCVM model. Model parameters either are taken from the literature (when they are available) or are determined in this work through the regression of binary and ternary vapor-liquid equilibrium data. Accurate predictions are obtained with the new model over a wide range of temperatures, pressures, MDEA concentrations, and loadings. |
en |
heal.publisher |
AMER CHEMICAL SOC |
en |
heal.journalName |
Industrial and Engineering Chemistry Research |
en |
dc.identifier.doi |
10.1021/ie030769v |
en |
dc.identifier.isi |
ISI:000221586100023 |
en |
dc.identifier.volume |
43 |
en |
dc.identifier.issue |
11 |
en |
dc.identifier.spage |
2798 |
en |
dc.identifier.epage |
2804 |
en |