| DB e HB | Diameter of cell, m Yield = 100 × mass of oil extracted/mass of solid phase (dimensionless) Height of cell, m |
| N | Mass of the solute, kg |
| TCER | Constant extraction period time, s |
|
| Volumetric mass transfer coefficient in the fluid phase, 1/s |
|
| Volumetric mass transfer coefficient in the solid phase, 1/s |
|
| Mass flowrate of solvent per unit mass of solid phase, 1/s |
| q | specific amount of solvent = Q/N (dimensionless) |
| qm qvol | Specific amount of solvent at the start of the extraction that occurs inside the trichomes Volumetric flowrate of CO2, m3/s |
| Q V | Amount of solvent used, kg Volume of cell, m3 |
| W | Parameter of slow-extraction period (dimensionless) |
| xk | Easily accessible concentration of a solute in solid substrate, kg/kg |
| x0 | Global yield, kg/kg |
| yr | Solubility, kg/kg |
| Z | Parameter of the Sovová’s model for the CER period |
| Greek letters | |
|
| Void fraction |
|
| Density of the solvent, kg/m3 |
|
| Density of the solid phase, kg/m3 |