Heat transfer together with phase
change in pipelines frequently
occurs in petroleum and chemical industries. Numerical methods have
been extensively used in modeling two-phase flow and become more complicated
when the phase change process is involved. One-dimensional two-fluid
models are unreliable for modeling phase behavior because they do
only yield uniform velocity/temperature distributions. Thus,
mathematical models based on bipolar coordinate systems have been
developed, where nonisothermal flows and heat/mass transfer have been
implemented to predict the varying vapor–liquid interface and
component mass fraction. The PR equation is chosen for phase equilibrium
calculation and the P–T flash
is used to evaluate the physical properties, gasification rate, and
enthalpy departure. The liquid holdup, velocity/temperature profile,
and phase fraction could be predicted along the pipeline, which are
important for transportation optimization and flow assurance. The
numerical predictions fit well with available experimental and simulated
data and could present more detailed and accurate results.