𝔖 Bobbio Scriptorium
✦   LIBER   ✦

The MHV2 model: Prediction of phase equilibria at sub- and supercritical conditions

✍ Scribed by Søren Dahl; Andrzej Dunalewicz; Aage Fredenslund; Peter Rasmussen


Publisher
Elsevier Science
Year
1992
Tongue
English
Weight
451 KB
Volume
5
Category
Article
ISSN
0896-8446

No coin nor oath required. For personal study only.

✦ Synopsis


MHV2 is a group-contribution equation-of-state based on the modified Huron-Vidal mixing rule. It combines the SRK equation-of-state with a model for the excess Gibbs energy, the modified UNIFAC model. It can be applied at all temperatures and pressures of interest in chemical process design and it is capable of reproducing the low pressure information given by the modified UNIFAC model.

In the present work, we have investigated the ability of the model to predict high pressure vapor-liquid equilibria (VLE), liquid-liquid equilibria (LLE), and three-phase equilibria for systems with mixed solvents together with supercritical gases and lighter alkanes. Considering the complexity of these mixtures, satisfactory results are obtained.


📜 SIMILAR VOLUMES


Multiphase equilibria of binary and tern
✍ D. Zhang; A. Cheung; B.C.-Y. Lu 📂 Article 📅 1992 🏛 Elsevier Science 🌐 English ⚖ 874 KB

The P-T-liquid composition values of the solid-liquid-gas coexistence curves were determined for the binary systems naphthalene-ethylene and biphenyl-ethylene using the first freezing point method. The technique was further extended to the determination of the P and T values of the solid-solid-liqui

Evaluation of a model for the prediction
✍ Anthony I. Kakhu; John Homer 📂 Article 📅 1996 🏛 Elsevier Science 🌐 English ⚖ 1008 KB

A model (AGAPE), based on consideration of the properties of whole, rather than segments of, molecules, that allows the prediction of phase equilibria in terms of two general physical parameters is presented. One of the parameters is a geometric (or entropic) parameter while the other is an energeti

Phase equilibria of the CO2–Jiangsu crud
✍ Z.M. Liu; G.Y. Yang; Y. Lu; B.X. Han; H.K. Yan 📂 Article 📅 1999 🏛 Elsevier Science 🌐 English ⚖ 134 KB

Phase equilibria of the supercritical (SC ) and subcritical CO 2 -Jiangsu crude oil systems were determined at 328.15 K and 348.15 K in the pressure range 0-16 MPa. The solubility of CO 2 in the crude oil increases with pressure and decreases with temperature. The solubility of the crude oil compone