| A |
area,
|
|
|
interfacial area concentration (IAC), 1/m |
| C |
coefficient |
|
|
drag coefficient |
|
|
inter-group transfer coefficient |
| Ca |
Capillary number |
|
|
|
|
-
|
adjustable parameters |
| D |
bubble size, m |
|
|
critical diameter for transition between bubble groups, m |
|
|
bubble critical size due to phase change, m |
|
|
hydraulic diameter of the flow channel, m |
|
|
an arbitrarily defined minimum eddy size, m |
|
|
surface equivalent diameter, m |
|
|
Sauter mean diameter, m |
|
|
diameter of bubble 1, m |
|
|
diameter of bubble 2, m |
| d |
parent bubble diameter, m |
|
|
daughter bubble diameter, m |
|
|
eddy size, m |
| E |
kinetic energy, kg
|
| F(α) |
turbulence damping factor due to the presence of the gas phase |
| f |
frequency, 1/s |
|
|
volume fraction,
|
| G |
gap in a rectangular/annular channel, m |
| g |
gravitational acceleration, m/
|
| I |
turbulent intensity |
| j |
superficial velocity, m/s |
| K |
constant |
| k |
the ratio of the average turbulent eddy size to the bubble Sauter mean diameter |
|
|
average distance between bubbles, m |
| N |
average number of eddies arrive at the surface of a drop in unit time |
| n |
number density of bubbles or eddies, 1/
|
| R |
source/sink rates per unit mixture volume, 1/
|
|
|
radius of the tube, m |
| r |
bubble radius, m |
| S |
source/sink rates per unit mixture volume, 1/
|
| t |
time, s |
|
|
relative velocity between bubbles, m/s |
|
|
wake velocity of Group II bubbles, m/s |
|
|
wake velocity of Group I bubbles, m/s |
| V |
volume,
|
| v |
velocity, m/s |
|
|
volume influenced by a wake,
|
|
|
interfacial velocity, m/s |
|
|
the average local particle velocity, m/s |
| We Weber number |
| Greek symbols |
|
|
volume fraction, packing limit |
|
|
factor considering the effect of the size ratio between bubbles and eddies |
|
|
shear rate, 1/s |
|
|
factor considering the effect of the bubble that reduces the free space for bubble movement and causes an increase in the collision frequency. |
|
|
energy dissipation rate, /
|
| η |
efficiency |
|
|
rate of volume source per unit mixture volume, 1/s |
|
|
mass generation rate, kg/s |
|
|
IAC source/sink rate, 1/ms |
|
|
liquid viscosity, Pa·s |
| ν |
kinetic viscosity, /
|
| ρ |
density, kg/
|
| Π |
factor considering the ratio of the mean bubble distance to the turbulent path length |
|
|
surface tension, N/m |
|
|
surface tension forces, N |
|
|
viscous stress, N |
|
|
factor depending on bubble shape |
|
|
inter-group transfer coefficient |
| Subscripts |
| 1 |
Group I |
| 2 |
Group II |
| b |
breakup |
| c |
coalescence |
| coll |
collision |
| cr |
critical value |
| D |
drag force |
| d |
dispersed |
| e |
eddy |
| f |
liquid phase |
| g |
gas phase |
| i |
i-th component |
| j |
j-th component |
| kin |
kinetic |
| m |
mixture value |
| max |
maximum |
| max2 |
maximum in Group II |
| min |
minimum |
| nuc |
nucleation |
| ph |
phase change |
| RC |
random collision mechanism |
| SO |
shearing-off mechanism |
| TI |
turbulent impact mechanism |
| WE |
wake entrainment mechanism |
| SI |
surface instability mechanism |
| Superscripts |
| * non-dimensional value |
| (1) |
interactions within Group I bubbles |
| (11, 2) |
coalescence of a Group I bubble with another Group I bubble to generate a Group II bubble |
| (12, 2) |
coalescence of a Group I bubble with a Group II bubble to generate a new Group II bubble |
| (2) |
interactions within Group II bubbles |
| (2, 1) |
Group I bubbles generated from breakup of a Group II bubble |
| (2, 2) |
Group II bubbles generated from breakup of a Group II bubble |
| (2, 11) |
breakup of a Group II bubble to generate two Group I bubbles |
| (2, 12) |
breakup of a Group II bubble to generate a (or multiple) Group I bubble(s) and a Group II bubble |