dc.contributor.author |
Voutsas, E |
en |
dc.contributor.author |
Lampadariou, M |
en |
dc.contributor.author |
Magoulas, K |
en |
dc.contributor.author |
Tassios, D |
en |
dc.date.accessioned |
2014-03-01T01:18:15Z |
|
dc.date.available |
2014-03-01T01:18:15Z |
|
dc.date.issued |
2002 |
en |
dc.identifier.issn |
0378-3812 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/14887 |
|
dc.subject |
Normal boiling point |
en |
dc.subject |
Prediction |
en |
dc.subject |
Pure |
en |
dc.subject |
Vapor pressure |
en |
dc.subject.classification |
Thermodynamics |
en |
dc.subject.classification |
Chemistry, Physical |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Alcohols |
en |
dc.subject.other |
Errors |
en |
dc.subject.other |
Thermal effects |
en |
dc.subject.other |
Boiling point |
en |
dc.subject.other |
Vapor pressure |
en |
dc.subject.other |
acid |
en |
dc.subject.other |
alcohol derivative |
en |
dc.subject.other |
aldehyde derivative |
en |
dc.subject.other |
alkadiene |
en |
dc.subject.other |
alkane derivative |
en |
dc.subject.other |
alkene derivative |
en |
dc.subject.other |
alkyne derivative |
en |
dc.subject.other |
amine |
en |
dc.subject.other |
aromatic hydrocarbon |
en |
dc.subject.other |
ester derivative |
en |
dc.subject.other |
ether derivative |
en |
dc.subject.other |
glycol |
en |
dc.subject.other |
halogen |
en |
dc.subject.other |
ketone derivative |
en |
dc.subject.other |
nitrogen derivative |
en |
dc.subject.other |
sulfur derivative |
en |
dc.subject.other |
boiling |
en |
dc.subject.other |
prediction |
en |
dc.subject.other |
temperature |
en |
dc.subject.other |
vapor pressure |
en |
dc.subject.other |
analytical error |
en |
dc.subject.other |
article |
en |
dc.subject.other |
methodology |
en |
dc.subject.other |
prediction |
en |
dc.subject.other |
temperature measurement |
en |
dc.subject.other |
vapor pressure |
en |
dc.title |
Prediction of vapor pressures of pure compounds from knowledge of the normal boiling point temperature |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/S0378-3812(01)00736-1 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/S0378-3812(01)00736-1 |
en |
heal.language |
English |
en |
heal.publicationDate |
2002 |
en |
heal.abstract |
A simple method for the prediction of vapor pressures of pure compounds from knowledge of the normal boiling point temperature is presented. Typical errors down to 10(-5) bar (1 Pa) are below 20% and are off only by a factor of 2-3 down to 10(-9) bar (10(-4) Pa), which must be considered very satisfactory considering the simplicity of the method and the uncertainty in the very low vapor pressure data. For higher pressures. up to 5 bar, very satisfactory results are obtained with typical errors below 3% but somewhat higher for alcohols. (C) 2002 Elsevier Science B.V. All rights reserved. |
en |
heal.publisher |
ELSEVIER SCIENCE BV |
en |
heal.journalName |
Fluid Phase Equilibria |
en |
dc.identifier.doi |
10.1016/S0378-3812(01)00736-1 |
en |
dc.identifier.isi |
ISI:000175678300007 |
en |
dc.identifier.volume |
198 |
en |
dc.identifier.issue |
1 |
en |
dc.identifier.spage |
81 |
en |
dc.identifier.epage |
93 |
en |