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Bubble point measurements of the system butane + octylbenzene in the temperature range 290-450 K

As a part of research on nitrogen displacement in light-oil reservoirs, the phase behavior of mixtures of a model oil and nitrogen is studied. The model oil consists of methane, butane, and tetradecane or octylbenzene. For reliable phase behavior calculations in the multicomponent system at reservoi...

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Bibliographic Details
Published in:Journal of chemical and engineering data 1994-01, Vol.39 (1), p.143-146
Main Authors: de Leeuw, Valentijn V, Poot, Wim, de Loos, Theo W, de Swaan Arons, Jakob
Format: Article
Language:English
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Summary:As a part of research on nitrogen displacement in light-oil reservoirs, the phase behavior of mixtures of a model oil and nitrogen is studied. The model oil consists of methane, butane, and tetradecane or octylbenzene. For reliable phase behavior calculations in the multicomponent system at reservoir conditions -- about 370 K and 50 MPa in the North Sea -- measurements are needed of at least the binary sub-systems in the temperature and pressure range of interest, in order to determine binary interaction coefficients. Bubble points of butane + octylbenzene at eight different mole fractions have been determined at 290--440 K using the synthetic method. The raw experimental data have been fitted using the Peng-Robinson and the Soave-Redlich-Kwong equations of state in combination with a number of different mixing rules.
ISSN:0021-9568
1520-5134
DOI:10.1021/je00013a040