1986
DOI: 10.1021/i200033a041
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Multicomponent vapor-liquid equilibria measurements for the development of an extractive distillation process for the processing of gas issuing from a carbon dioxide/EOR project

Abstract: This paper presents V-L-E data for a multicomponent C02-rich gas added to n-pentane at a series of fixed temperatures to produce an equilibrium mixture of various fixed total pressures to form a quasi-binary system containing compounds such as C02, C2H6, C3K8, H2S, n-C4H10, and n-C5H12. The experimental results provide data useable to adjust parameters and test for "proof of correlations". It suggests when the relative volatility ratios of the key components become unfavorable for LPG recovery and when the ove… Show more

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Cited by 8 publications
(3 citation statements)
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“…The less crucial vapor-liquid equilibria behavior representative of the bottom half of the column was not obtained in this study as it is represented by the higher temperature methane-free mixtures investigated in the previous studies (Hong and Kobayashi, 1986a).…”
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confidence: 96%
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“…The less crucial vapor-liquid equilibria behavior representative of the bottom half of the column was not obtained in this study as it is represented by the higher temperature methane-free mixtures investigated in the previous studies (Hong and Kobayashi, 1986a).…”
mentioning
confidence: 96%
“…The K values of H2S, an intermediate component, are scarcely affected by the presence of methane, at the pressures studied in this investigation. Even the n-pentane losses may be expected to be less, at the same pressure and temperature, than for the methane-free mixtures (Hong and Kobayashi, 1986a).…”
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confidence: 97%
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