Title of article
Predict heat of vaporization of crudes and pure components: Revised II
Author/Authors
Gopinathan، نويسنده , , Nishanth and Saraf، نويسنده , , Deoki.N، نويسنده ,
Issue Information
روزنامه با شماره پیاپی سال 2001
Pages
8
From page
277
To page
284
Abstract
Modeling of non-isothermal vapor–liquid equilibrium processes requires the availability of heat of vaporization data. An equation for calculation of heat of vaporization at normal boiling point has been developed which is particularly suited for pure hydrocarbons and petroleum fractions. The equation is simple to use and provides an improvement over the existing equations for pure hydrocarbons in wide boiling range. The equation is equally valid for crude oils, thus enabling the estimation of heats of vaporization needed for modeling of distillation units in oil refineries.
Keywords
Method of Calculation , Vapor–liquid equilibria , Hydrocarbons , Heat of Vaporization
Journal title
Fluid Phase Equilibria
Serial Year
2001
Journal title
Fluid Phase Equilibria
Record number
1983130
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