| Symbol | |
| C 2 | inertial resistance factor, m−1 |
| Cp,s | adsorbent specific heat capacity, J kg−1 k−1 |
| dp | particle diameter, m |
| D | diameter, m |
| Di,m | effective diffusion coefficient for component i, m2 s−1 |
| Di,j | diffusion coefficient of component i in component j, m2 s−1 |
| E | total energy of gas, J m−3 |
| E t1~t2 | energy consumption between t1 and t2 |
| h | enthalpy |
| hf | heat transfer coefficient between gas phase and solid, W m−2 K−1 |
| ∆H | the heat of adsorption, J mol−1 |
| J | diffusion flux, kg m−2 s−1 |
| keq | isotherm adsorption constant, Pa−1 |
| k 0 | adsorption constant at infinite dilution, Pa−1 |
| kL | LDF adsorption time constant, s−1 |
| k | thermal conductivity of gas |
| ks | adsorbent thermal conductivity, W m−1 K−1 |
| L | length, m |
| M | molecular weight, mol kg−1 |
| m | mass of captured, kg |
| n | heterogeneity parameter |
| p | Pressure, Pa |
| q | adsorption uptake, mol kg−1 |
| q* | equilibrium adsorption uptake, mol kg−1 |
| qm | maximum adsorption uptake, mol kg−1 |
| R | universal gas constant, J mol−1 K−1 |
| Sg | entropy generation, J K−1 |
| Smomentum | momentum source term |
| T | temperature, K |
| t | time, s |
| x | mole fraction |
| y | mass fraction |
| Greek letters | |
| α | permeability m2 |
| ε | porosity |
| ρ | density, kg m−3 |
| σ | entropy generation rate, W m3 K−1 |
| μ | gas dynamic viscosity, Pa s |
| μa | chemical potential of adsorbed phase, J kg−1 |
| μg | chemical potential of gas, J kg−1 |
| δ | bed wall thickness, m |
| τ | stress tensor |
| χ | chemical potential of gas in diffusion process, J kg−1 |
| Subscripts | |
| a | adsorbed phase |
| ad | adsorption |
| b | bed |
| c | critical |
| d | diffusion |
| g | gas |
| i | components |
| in | inlet |
| p | particle |
| q | heat transfer |