✦ LIBER ✦

Prediction of phase equilibria using the Redlich?Kwong equation of state

✍ Scribed by Stead, Keith; Williams, John M.

Book ID: 121254930
Publisher: The Royal Society of Chemistry
Year: 1980
Weight: 277 KB
Volume: 76
Category: Article
ISSN: 0300-9238
DOI: 10.1039/F29807601045

No coin nor oath required. For personal study only.

📜 SIMILAR VOLUMES

Prediction of Phase Equilibria in Sour N

Prediction of Phase Equilibria in Sour Natural Gas Systems Using the Soave-Redlich-Kwong Equation of State

✍ Evelein, Katherine A.; Moore, R. Gordon 📂 Article 📅 1979 🏛 American Chemical Society ⚖ 678 KB

Comparison of the Peng−Robinson and Soav

Comparison of the Peng−Robinson and Soave−Redlich−Kwong Equations of State Using a New Zero-Pressure-Based Mixing Rule for the Prediction of High-Pressure and High-Temperature Phase Equilibria

✍ Twu, Chorng H.; Coon, John E.; Bluck, David 📂 Article 📅 1998 🏛 American Chemical Society 🌐 English ⚖ 52 KB

Phase equilibria calculations with a mod

Phase equilibria calculations with a modified redlich-kwong equation of state

✍ M. S. Medani; M. A. Hasan 📂 Article 📅 1978 🏛 John Wiley and Sons 🌐 English ⚖ 580 KB

Prediction of Liquid Phase Enthalpies wi

Prediction of Liquid Phase Enthalpies with the Redlich-Kwong Equation of State

✍ Joffe, Joseph; Zudkevitch, David 📂 Article 📅 1970 🏛 American Chemical Society ⚖ 412 KB

Vapor-liquid equilibria with the redlich

Vapor-liquid equilibria with the redlich-kwong equation of state

✍ Joseph Joffe; George M. Schroeder; David Zudkevitch 📂 Article 📅 1970 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 323 KB 👁 2 views

Correlation and prediction of vapor-liqu

Correlation and prediction of vapor-liquid equilibria with the redlich-kwong equation of state

✍ David Zudkevitch; Joseph Joffe 📂 Article 📅 1970 🏛 American Institute of Chemical Engineers 🌐 English ⚖ 810 KB

A modified Redlich-Kwong equation has been applied to the calculation of phase equilibria in multicomponent systems. The two parameters of the Redlich-Kwong equation are treated as temperature functions. They are obtained for each pure component from experimental vapor pressures and liquid densities