| A |
Membrane surface (m) |
| CFD |
Computational fluid dynamic |
| Ci
|
Concentration of component i (mol/m3) |
| CH2O,permeate
|
Water concentration in the permeate side |
| CH2O,retentate
|
Water concentration in the permeate side |
| dcat
|
Diameter of catalyst particle (m) |
|
|
Single-phase diffusion coefficients (m2/s) |
|
|
The effective diffusion in porous media(m2/s) |
| E1
|
Activation energy (kJ/mol) |
| E2
|
Activation energy (kJ/mol) |
| Et |
Ethanol |
| EtLA |
Ethyl levulinate |
| JH2O
|
Water permeating flux (mol/m2/s) |
| J0,H2O
|
Water permeability |
| K |
Equilibrium constant (-) |
| k1,0
|
Rate constant ((m3/mol)2/s) |
| k2,0
|
Rate constant ((m3/mol)(m3/kg)/s) |
| Kbr
|
Permeability (m2) |
| Kref
|
Equilibrium cst (-) |
| LA |
Levulinic acid |
| LA-ESR |
Livulinic acid esterification |
|
|
Molecular weight of component i (mol/g) |
| NOx |
Nitrogen oxides |
| PV |
Pervaporation |
| PVA |
Poly(vinyl alcohol) |
| PVMR |
Pervaporation membrane reactor |
| ri
|
Reaction rate of component i (mol/m3/s) |
| Si
|
Sink/source term of component i (kg/m3/s) |
| SOx
|
Sulfur oxides |
| Tref
|
Temperature ref (K) |
| u |
Velocity (m/s) |
| V |
Computational cell volume (m3) |
| Vi
|
Molar volume at normal boiling point (cm3/mol) |
| W |
Weight of catalyst (g) |
|
|
Forchheimer coefficient |
|
|
Enthalpy (kJ/mol) |
|
|
(-) |
|
|
Viscosity (cP) |
| µmix
|
Viscosity reaction mixture (cP) |
|
|
Density (kg/m3) |
|
|
Catalyst density (kg/m3) |
| τ |
Tortuosity |
| ϕ |
Association factor (-) |