Currently, no comprehensive mechanistic model for the two-phase flow t
hrough a swirl vane steam separator is available. Therefore, an attemp
t has been made to develop an analytical model, using fundamental flui
d mechanics, which is capable of predicting separator performance over
a wide range of conditions. The developed model subdivides a typical
boiling water reactor swirl vane steam separator into four distinct re
gions. the standpipe region, the swirl vane region, the transition reg
ion, and the free vortex region. In each region, the vapor and liquid
components are treated separately and the behavior of individual dropl
ets is determined from the drag force induced by the vapor continuum.
The analytical model is used to first determine the vapor velocities t
hroughout the separator. The drag force on the droplets is then determ
ined, and the droplets are tracked through the separator in order to d
etermine the exit position of each droplet. Separator performance can
then be determined from this final position in terms of the fraction o
f droplets removed from the flow stream. In order to assess the validi
ty of this model, the computer code SEPARATOR was developed. Among oth
er capabilities, the code is capable of determining separator performa
nce in terms of carryover, carry under, and exit quality. However, due
to the simplicity of the single-phase fluid treatment of the vapor co
ntinuum and the lack of data related to the average droplet diameter f
or flows of this nature, the results are not of significant quantitati
ve value. The investigation performed does, however, suggest that the
developed methodology, upon refinement of the single-phase fluids trea
tment, will yield quantitatively accurate results for nearly all separ
ator operating conditions of interest.