dc.contributor.author |
Avlonitis, G |
en |
dc.contributor.author |
Mourikas, G |
en |
dc.contributor.author |
Stamataki, S |
en |
dc.contributor.author |
Tassios, D |
en |
dc.date.accessioned |
2014-03-01T01:09:39Z |
|
dc.date.available |
2014-03-01T01:09:39Z |
|
dc.date.issued |
1994 |
en |
dc.identifier.issn |
0378-3812 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/11128 |
|
dc.subject |
Empirical |
en |
dc.subject |
Hydrocarbons |
en |
dc.subject |
Interaction parameter |
en |
dc.subject |
Methods of calculation |
en |
dc.subject |
Nitrogen |
en |
dc.subject |
Theory |
en |
dc.subject.classification |
Thermodynamics |
en |
dc.subject.classification |
Chemistry, Physical |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.other |
Interaction |
en |
dc.subject.other |
Mixtures |
en |
dc.subject.other |
Nitrogen-Hydrocarbon |
en |
dc.subject.other |
Aromatic compounds |
en |
dc.subject.other |
Correlation methods |
en |
dc.subject.other |
Equations of state |
en |
dc.subject.other |
Hydrocarbons |
en |
dc.subject.other |
Nitrogen compounds |
en |
dc.subject.other |
Phase equilibria |
en |
dc.subject.other |
Pressure effects |
en |
dc.subject.other |
Thermal effects |
en |
dc.subject.other |
Interaction coefficients |
en |
dc.subject.other |
Translated modified Peng-Robinson equation of state |
en |
dc.subject.other |
Binary mixtures |
en |
dc.title |
A generalized correlation for the interaction coefficients of nitrogenhydrocarbon binary mixtures |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/0378-3812(94)02554-1 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/0378-3812(94)02554-1 |
en |
heal.language |
English |
en |
heal.publicationDate |
1994 |
en |
heal.abstract |
The present study introduces a generalized correlation for the interaction coefficients of N2(i)/hydrocarbon(j) binary systems as a function of the reduced temperature of nitrogen (T(ri)) and the acentric factor of the hydrocarbon (omega(j)). It is applicable to the translated-modified Peng-Robinson equation of state (t-mPR EoS) and the original PR as well. The prediction results for N2/n-alkane binary systems are satisfactory with an average absolute error in bubble-point pressure below 6%. Equally good results are obtained for the binaries of N2 with naphthenes, iso-alkanes and aromatics. Use of temperature independent interaction coefficients is recommended for the N2/alkene systems. The proposed correlation is limited to pressures lower than 500 bar, and gives better prediction than those reported previously. |
en |
heal.publisher |
ELSEVIER SCIENCE BV |
en |
heal.journalName |
Fluid Phase Equilibria |
en |
dc.identifier.doi |
10.1016/0378-3812(94)02554-1 |
en |
dc.identifier.isi |
ISI:A1994PX51800004 |
en |
dc.identifier.volume |
101 |
en |
dc.identifier.issue |
C |
en |
dc.identifier.spage |
53 |
en |
dc.identifier.epage |
68 |
en |