A method for evaluation of the critical velocity in the case of two (vapor-
liquid)-phase mixtures transported in pipelines was developed. This method
is based on a theoretical background of complex hydrocarbon mixture thermod
ynamics with respect to application in the petrochemical industry. Methods
published so far have focused on applications ill the power industry, where
the water-steam two-phase system is considered. The method presented allow
s one to calculate pressure drop, velocity, and temperature profiles for tw
o-phase complex hydrocarbon systems and to identify the critical flow prese
nce. In this method the critical condition means a singular discontinuity w
here the finite pressure and/or velocity change corresponds to an infinites
imal change in space coordinate. An. example of applying the method in the
case of a furnace-to-distillation column transfer line is shown. It can be
observed that using this method can be considered a col contribution to sol
ving practical industrial cases. This method was verified in industrial pra
ctice for a long time and satisfactory results wets obtained.