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High-pressure vapor-liquid equilibria involving mixtures of nitrogen, carbon dioxide, and eta-butane

Journal Article · · Journal of Chemical and Engineering Data; (USA)
DOI:https://doi.org/10.1021/je00057a011· OSTI ID:5298094
 [1];  [2]
  1. Du Pont de Nemours (E.I.) and Co., Wilmington, DE (USA). Technical Div.
  2. Delaware Univ., Newark, DE (USA). Dept. of Chemical Engineering
A new high-pressure vapor-liquid equilibrium apparatus has been constructed with the capability of measuring the compositions and densities of the coexisting equilibrium phases at constant temperature and/or pressure. This apparatus was tested with the carbon dioxide + n-butane system with excellent agreement observed between our results and previously published data. Data are also reported for the nitrogen + n-butane system and the previously unmeasured nitrogen + carbon dioxide + n-butane system. These data were modeled with the Peng-Robinson equation of state. Excellent fits were obtained for the compositions in the carbon dioxide + n-butane system, but a poor fit was obtained for the nitrogen + n-butane data. The ability of the Peng-Robinson equation of state to accurately predict the phase behavior of the ternary mixture is dependent on the fits of the binary data, and therefore the ternary data are also not fit well. In all cases the liquid densities are poorly predicted with the Peng-Robinson equation of state.
OSTI ID:
5298094
Journal Information:
Journal of Chemical and Engineering Data; (USA), Journal Name: Journal of Chemical and Engineering Data; (USA) Vol. 34:3; ISSN JCEAA; ISSN 0021-9568
Country of Publication:
United States
Language:
English