Zobrazeno 1 - 6
of 6
pro vyhledávání: '"Nishawn S. M. Hanif"'
Publikováno v:
Fluid Phase Equilibria. 130:73-85
A model based upon the Peng-Robinson equation of state with the Wong-Sandler mixture combining rule (W-S MCR) can correlate phase equilibria in CO 2 + H 2 O. The W-S MCR requires two energy parameters for liquid behavior and one interaction parameter
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::79e2fe466593018560fd7bf6a9e54ff7
https://doi.org/10.1016/s0378-3812(96)03196-2
https://doi.org/10.1016/s0378-3812(96)03196-2
Publikováno v:
Fluid Phase Equilibria. 126:53-70
We have used an efficient, new Gibbs minimization method with an equation of state (EOS) model to predict phase equilibria for hydrocarbon water binary mixtures. The method utilizes the observation by Eubank and Hall (1995) that a plot of the derivat
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::4f68a540df78e2035095cea05290ca1a
https://doi.org/10.1016/s0378-3812(96)03141-x
https://doi.org/10.1016/s0378-3812(96)03141-x
Publikováno v:
Industrial & Engineering Chemistry Research. 35:2431-2437
Cubic equations of state (EOS) cannot provide accurate multithermophysical properties over wide ranges of temperature and pressure for pure components in the fluid state. More complex, noncubic EOS are required, but only recently has their use been m
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::61f350e1f393a797e0fbfeaf730129b2
https://doi.org/10.1021/ie950681k
https://doi.org/10.1021/ie950681k
Publikováno v:
Industrial & Engineering Chemistry Research. 35:4348-4353
Eubank and Hall have shown recently that the tangent-line criterion reduces to an equal area construction for the derivative of the total Gibbs energy plotted against composition. This paper presents another criterion along with a thermodynamic proof
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::494d05e149a6438b886f3b27eab17c8e
https://doi.org/10.1021/ie960203p
https://doi.org/10.1021/ie960203p
Autor:
Philip T. Eubank, Nishawn S. M. Hanif, Juan F. J. Alvarado, Kenneth R. Hall, Guor-Shiarn Shyu
Publikováno v:
Industrial & Engineering Chemistry Research. 34:4562-4570
The phase equilibrium behavior of fluid mixtures is an important design consideration for both chemical processes and oil production. Eubank and Hall have recently shown the equal area rule (EAR) applies to the composition derivative of the Gibbs ene
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::2760976fd0f3d2044e361170c219ae60
https://doi.org/10.1021/ie00039a051
https://doi.org/10.1021/ie00039a051
Publikováno v:
Industrial & Engineering Chemistry Research. 34:314-323
New procedures are developed for use with the recent Wong-Sandler mixing rules for the prediction of mixture phase equilibria from cubic equations of state. Improvements in the apriori evaluation of both the liquid-phase parameter A[sub [infinity]][s
Externí odkaz:
https://explore.openaire.eu/search/publication?articleId=doi_________::d3db7780dfd0e3e344bcb76c7a911e00
https://doi.org/10.1021/ie00040a034
https://doi.org/10.1021/ie00040a034