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Total-pressure vapor-liquid equilibrium data for binary systems of dichloromethane with pentane, acetone, ethyl acetate, methanol, and acetonitrile

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This article is published in Journal of Chemical & Engineering Data.The article was published on 1983-10-01. It has received 16 citations till now. The article focuses on the topics: Pentane & Ethyl acetate.

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Application of a volume-translated Peng-Robinson equation of state on vapor-liquid equilibrium calculations

TL;DR: In this paper, a volume-translated Peng-Robinson (VTPR) equation of state (EOS) was developed, where the temperature dependence of the EOS energy parameter was regressed by an improved expression which yields better correlation of purefluid vapor pressures.
Journal ArticleDOI

Generalized binary interaction parameters for the Peng–Robinson equation of state

TL;DR: In this article, the authors developed reliable generalized models to estimate the BIPs for the PR EOS using a quantitative structure-property relationship (QSPR) modeling approach.
Journal ArticleDOI

Vapor Pressures of Acetonitrile Determined by Comparative Ebulliometry

TL;DR: In this paper, the vapor pressure of acetonitrile has been measured over the temperature and pressure range of 278 K and 4.3 kPa to 540 K. The results have been correlated using generalized Wagner equations, a key feature of which is the use of the reversed reduced temperature = 1 - T/Tc where Tc is the critical temperature.
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A cubic equation of state for vapor-liquid equilibrium calculations of nonpolar and polar fluids

TL;DR: In this article, a cubic perturbed hard body (CPHB) equation of state (EOS) was developed and applied for vapor-liquid equilibrium (VLE) calculations in this study.
Journal ArticleDOI

Dichloromethane: Revision and extension of pρT relationships for the liquid

TL;DR: In this article, the Tait equation was combined with other values existing in the literature, which made it possible to extend the information on the saturated liquid density to the range T ǫ(208 to 399) K.
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