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.
Hydrocarbon vapor-liquid equilibria and solubility parameter
โ Scribed by J. M. Prausnitz; W. C. Edmister; K. C. Chao
- Publisher
- American Institute of Chemical Engineers
- Year
- 1960
- Tongue
- English
- Weight
- 650 KB
- Volume
- 6
- Category
- Article
- ISSN
- 0001-1541
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๐ SIMILAR VOLUMES
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
## Abstract Experimental equilibrium vapor and liquid compositions are reported for the hydrogenโmethane system at โ150ยฐ, โ200ยฐ, and โ250ยฐF. and at pressures of 500 to 4,000 lb./sq. in. The ternary system hydrogenโmethaneโpropane was studied at 0ยฐ, โ100ยฐ, and โ200ยฐF. at 500 and 1,000 lb./sq. in. Ph