VAPOR-LIQUID-EQUILIBRIA FOR THE TERNARY-SYSTEM N-2-C4H10 AT 250 AND 270 K(CO2+N)

Authors
BROWN TS SLOAN ED KIDNAY AJ
Citation
Ts. Brown et al., VAPOR-LIQUID-EQUILIBRIA FOR THE TERNARY-SYSTEM N-2-C4H10 AT 250 AND 270 K(CO2+N), International journal of thermophysics, 15(6), 1994, pp. 1211-1219
Citations number
4
Categorie Soggetti
Physics, Applied","Chemistry Physical
Journal title
International journal of thermophysics → ACNP
ISSN journal
0195928X
Volume
15
Issue
6
Year of publication
1994
Pages
1211 - 1219
Database
ISI
SICI code
0195-928X(1994)15:6<1211:VFTTNA>2.0.ZU;2-L
Abstract
The system studied was nitrogen + carbon dioxide + n-butane at 250 and 270 K and at pressures from 1.5 to 14 MPa. The Peng-Robinson equation was used to model the results, since it is the most widely accepted e quation of state in the gas processing industry. In general, the predi ctions are most accurate at low and moderate pressures and poorest at high pressures, especially near the critical region.