|
|
velocity vector (m/s) |
|
|
pressure (Pa) |
|
|
gravity vector (m/s2) |
|
|
external force (N) |
|
|
diffusion flux (kg/m2·s−1) |
|
|
diffusion coefficient(m2/s) |
|
|
concentration of phase i (mol/L) |
|
|
mixing index (−) |
|
|
concentration of ethanol of sampling point (mol/L) |
|
|
average concentration of ethanol of cross-section (mol/L) |
|
|
extraction efficiency (−) |
|
|
volume ratio of water to n-butanol (−) |
|
|
partition coefficient (−) |
|
KLa
|
volumetric mass transfer coefficient (s−1) |
|
|
concentration of succinic acid in the water phase at the inlet (mol/L) |
|
|
concentration of succinic acid in the water phase at the outlet (mol/L) |
|
|
concentration of succinic acid in the organic phase at the inlet (mol/L) |
|
|
equilibrium concentration of succinic acid in the water phase (mol/L) |
|
|
equilibrium concentration of succinic acid in the organic phase (mol/L) |
|
|
hydraulic diameter at the inlet (m) |
| Greek symbols |
|
|
volume fraction of phase i (−) |
|
|
density of phase i (kg/m3) |
|
|
average density (kg/m3) |
|
|
water phase density (kg/m3) |
|
|
organic phase density (kg/m3) |
|
|
viscosity (Pa·s) |
|
|
viscosity (Pa·s) |
|
|
water phase viscosity (Pa·s) |
|
|
organic phase viscosity (Pa·s) |
|
|
residence time (s) |
| Dimensionless numbers |
|
Re
|
Reynolds number (−) |