Sloshing
behaviors in liquid containers have been thoroughly studied
for several decades by both experiments and numerical simulations.
However, very few efforts are devoted to address the performance of
gas pretreatment system of FLNG (floating liquefied natural gas) plants,
particularly for the liquid entrainment estimation in the gas phase
of multiphase separators. In this work, a multiscale simulation method
was performed to study the sloshing impact on gas pretreatment for
FLNG plants. First, computational fluid dynamics (CFD) simulations
were performed to quantify liquid entrainment for oil–gas separator
under sloshing. Next, CFD results were utilized by the gas pretreatment
process modeling, where flow maldistribution in the oil–gas
separator and absorption column due to sloshing was coupled with steady-state
process simulations. Results show that the sloshing behavior increases
the amount of liquid carryover into the gas phase substantially, while
the performance of the gas pretreatment system decreases consequently.