Modeling the High-Pressure Ammonia−Water System with WATAM and the Peng−Robinson Equation of State for Kalina Cycle Studies
- 19 March 1998
- journal article
- research article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 37 (5), 1644-1650
- https://doi.org/10.1021/ie970638s
Abstract
No abstract availableKeywords
This publication has 19 references indexed in Scilit:
- Vapor-liquid equilibrium data for the ammonia-water system and its description with a modified cubic equation of stateJournal of Chemical & Engineering Data, 1991
- Vapor-liquid equilibria for the system ammonia + water up to the critical regionJournal of Chemical & Engineering Data, 1990
- Vapor-liquid equilibria in the ammonia-water systemJournal of Chemical & Engineering Data, 1987
- Correlation of ammonia-water equilibrium data with various modified Peng-Robinson equations of stateFluid Phase Equilibria, 1986
- New Mixing Rule for Cubic Equations of State for Highly Polar, Asymmetric SystemsPublished by American Chemical Society (ACS) ,1986
- Vapor-liquid equilibrium data for the binary system water-ammonia at 403.1, 453.1, and 503.1 K up to 7.0 MPaJournal of Chemical & Engineering Data, 1985
- Two- and Three-Phase Equilibrium Calculations for Coal Gasification and Related ProcessesPublished by American Chemical Society (ACS) ,1980
- A New Two-Constant Equation of StateIndustrial & Engineering Chemistry Fundamentals, 1976
- Vapor-liquid equilibriums in system ammonia-water at 14.69 and 65 psiaJournal of Chemical & Engineering Data, 1975
- Improved equation for prediction of saturated liquid densityJournal of Chemical & Engineering Data, 1972