| A | Clausius–Claperon equation constant |
| Ca | specific heat capacity of the adsorbent, kJ·kg−1·K−1 |
| C lc | specific heat capacity of water, kJ·kg−1·K−1 |
| Cm | specific heat capacity of stainless steel, kJ·kg−1·K−1 |
| hd | desorption heat, kJ·kg−1·K−1 |
| L | latent heat of vaporization of water, kJ·kg−1 |
| Ma | adsorbent mass, kg |
| Mm | adsorption bed mass, kg |
| Qc | heat taken away during cooling of adsorption bed, kJ·kg−1 |
| Qeva | sensible heat of liquid refrigerant from Tc to evaporation temperature Te, kJ·kg−1 |
| Qg | heat absorbed during the desorption process, kJ·kg−1 |
| Qref | cooling capacity, kJ·kg−1 |
| R | universal gas constant, J·mol−1·K−1 |
| Ta1 | initial adsorption temperature, K |
| Ta2 | adsorption temperature, K |
| Tc | condensation temperature, K |
| Te | evaporation temperature, K |
| Tg1 | initial desorption temperature, K |
| Tg2 | desorption temperature, K |
| Tsat | saturation temperature corresponding to the adsorption pressure, K |
| xconc | water adsorption capacity in gas–solid-phase equilibrium at the time of adsorption in adsorption temperature, kg·kg−1 |
| xdil | water adsorption capacity in gas–solid-phase equilibrium at the time of desorption in desorption temperature, kg·kg−1 |
| x0 | maximum adsorption capacity, kg·kg−1 |
| Δx | circulating adsorption capacity, kg·kg−1 |