1969
DOI: 10.1021/je60043a025
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Vapor-liquid equilibriums of 1,3-butadiene systems

Abstract: was used without further purification, since it had a melting point of 2.5°± 0.1°C ., which was in good agreement with the literature value of 2.55°C. (5).A known excess of salt was added to a selected mixture of water and formamide in a 100-ml. volumetric flask. Each flask was attached to the arm of a mechanical shaker and immersed in a water bath which was maintained at 25°C.

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Cited by 22 publications
(3 citation statements)
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“…The ability of the analytical expressions for GE to fit the experimental pressure data, as shown in Table VI, substantiates results reported by others (5,14); the Wilson equation is the best of the two-parameter equations, often superior to higher order Redlich-Kister expressions.…”
Section: Discussionsupporting
confidence: 86%
“…The ability of the analytical expressions for GE to fit the experimental pressure data, as shown in Table VI, substantiates results reported by others (5,14); the Wilson equation is the best of the two-parameter equations, often superior to higher order Redlich-Kister expressions.…”
Section: Discussionsupporting
confidence: 86%
“…Only the data of Wong and Eckert ( 1969) are available for comparison of butadiene solubilities in carbon disulfide and ethyl acetate. This comparison indicates our values are approximately 5%, and 0.1% lower in carbon disulfide.…”
Section: Resultsmentioning
confidence: 99%
“…The solubility of I -butene (Brooks and McKetta, 1955) and 1,3-butadiene (Reed and McKetta, 1959) in water were reported for various temperatures and pressures by McKetta and co-workers. The solubility of butadiene was also reported (Wong and Eckert, 1969) in seven solvents at 298.15 K and for a range of relatively low gas partial pressures. The latter data for two of the solvents provide a useful comparison for the results obtained in this work.…”
Section: X; = P / P ;mentioning
confidence: 94%