Vapor-liquid equilibria for C3 hydrocarbons
β Scribed by Arthur B. Hill; Robert H. McCormick; Paul Barton; M. R. Fenske
- Publisher
- American Institute of Chemical Engineers
- Year
- 1962
- Tongue
- English
- Weight
- 562 KB
- Volume
- 8
- Category
- Article
- ISSN
- 0001-1541
No coin nor oath required. For personal study only.
β¦ Synopsis
In calculating vapor-liquid equilibria for simple hydrocarbon systems ideal behavior is frequently assumed. The mill C. Paper W. Spalding Company, is presently Erie, Pennsylvania. with the Hammer-sumed that the reaction proceeded.
π SIMILAR VOLUMES
## Abstract Experimental equilibrium vapor and liquid compositions are reported for the hydrogenβmethane system at β150Β°, β200Β°, and β250Β°F. and at pressures of 500 to 4,000 lb./sq. in. The ternary system hydrogenβmethaneβpropane was studied at 0Β°, β100Β°, and β200Β°F. at 500 and 1,000 lb./sq. in. Ph
Generalized expressions are presented for Henry's constants and selfinteraction constants required in the Chueh-Prausnitz method for predicting the vapor-liquid equilibria for hydrogen and light hydrocarbon systems. The K-values calculated using the above correlations were compared with the K-values
Phase equilibrium data have been obtained for the binary systems nitrogen-argon and nitrogen-carbon monoxide at 8332Β°K. and for the systems nitrogen-methone, argon-methane, and carbon monoxide-methane at 90.67"K. Total pressures and compositions of both phases were measured. Parameters have been cal