Modeling of non-isothermal vapor-liquid equilibrium processes requires the
availability of heat of vaporization data. An equation for calculation of h
eat of vaporization at normal boiling point has been developed which is par
ticularly suited for pure hydrocarbons and petroleum fractions. The equatio
n 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 neede
d for modeling of distillation units in oil refineries. (C) 2001 Elsevier S
cience B.V. All rights reserved.