Multiphase and Volumetric Equilibria of the Ethane-Methanol System at Temperatures between -40° C. and 100° C.

Hua, Yi; Kohn, James P.

doi:10.1021/je60020a002

Search citation statements

Order By: Relevance

Paper Sections

Select...

Methods3

Citation Types

Supporting

Mentioning

Contrasting

Year Published

1966

1995

Publication Types

Select...

Article9

Relationship

Self Cite2

Independent7

Authors

Journals

Cited by 55 publications

(11 citation statements)

References 4 publications

Supporting

Mentioning

Contrasting

Order By: Relevance

“…The ethane (Matheson Co.) was pure grade, stated by the supplier to have 99 mole cc minimum purity, was purified before further use as described by Ma and Kohn (12), and was thought to have a purity of at least 99.7 mole c7c. Pure grade n-octane (Phillips Petroleum Co.) was stated by the supplier to be at least 99 mole % pure.…”

mentioning

confidence: 99%

Heterogeneous phase and volumetric equilibrium in the ethane-n-octane system

Rodrigues¹,

McCaffrey²,

Kohn³

1968

J. Chem. Eng. Data

Self Cite

View full text Add to dashboard Cite

mentioning

confidence: 99%

Heterogeneous phase and volumetric equilibrium in the ethane-n-octane system

Rodrigues¹,

McCaffrey²,

Kohn³

1968

J. Chem. Eng. Data

Self Cite

View full text Add to dashboard Cite

“…The ethane used in this study was the same grade and was prepurified the same as the ethane used in the previous study (12,16). It was thought to be 99.7 mole % ethane.…”

Section: Methodsmentioning

confidence: 99%

Heterogeneous phase equilibrium in the ethane-n-dodecane system

Lee¹,

Kohn²

1969

J. Chem. Eng. Data

View full text Add to dashboard Cite

of viscosity given by the present correlation and the values computed by Dean and Stiel's (3)equations. This may be attributed to inherent errors in the method of determination of the pseudocritical constants (3). In Figure 1, a regular trend is noticed between the limits of the two pure components. This clearly brings out the effect of mixture composition on viscosity of the Freon-12-Freon-22 vapor mixture system. CONCLUSIONThe present correlation facilitates design of engineering systems, as viscosity information on pure Freon-12 and Freon-22 vapors and their mixtures may be obtained readily. The determination of viscosity, however, requires an accurate knowledge of the temperature-dependence of viscosity at zero density. For engineering purposes, it may be convenient to use the atmospheric viscosity values. These atmospheric viscosity values may be calculated for pure components by the correlation of Witzell and Johnson (20) and for mixtures by Herning and Zipperer's (4) equation or by Wilke's (19) equation.

show abstract

“…3, 6). The experimental technique for obtaining composition data in the three phase region has been described by Ma (6) and Rodrigues (7).…”

Section: Methodsmentioning

confidence: 99%

Three phase equilibria in the binary systems ethane-n-docosane and ethane-n-octacosane

Rodrigues¹,

Kohn²

1967

J. Chem. Eng. Data

Self Cite

View full text Add to dashboard Cite

show abstract

Multiphase and Volumetric Equilibria of the Ethane-Methanol System at Temperatures between -40° C. and 100° C.

Abstract: The two-phase (vapor-liquid) P-V-T-X behavior and the three-phase (vapor-liquid 1, liquid 2) P-V-T-X behavior are presented at temperatures between -40°and 100°C.

Cited by 55 publications

References 4 publications

Heterogeneous phase and volumetric equilibrium in the ethane-n-octane system

Heterogeneous phase and volumetric equilibrium in the ethane-n-octane system

Heterogeneous phase equilibrium in the ethane-n-dodecane system

Three phase equilibria in the binary systems ethane-n-docosane and ethane-n-octacosane

Contact Info

Product

Resources

About