“…where С(x,y,τ) is the current volume concentration of the component in the fixed framework (in the gas located in the adsorbent pores and stagnant zones, around the adsorbent grains), [m 3 is the mass transfer coefficient between gas in the fixed framework and gas moving in cavities between grains of the adsorbent, D E is the equivalent value of the sorbate diffusion coefficient in the adsorbent grain, taking into account the diffusion features in the porous body: the relative pore volume, the variable pore cross section, the presence of dead-end pores, etc., [m 2…”