A new method for investigation of adsorption equilibrium and kinetics, named Nonlinear Frequency Response-Zero Length Column (NFR-ZLC) method, is introduced. It combines the advantages of the Nonlinear FR method (the potential to identify a model corresponding to the most probable kinetic mechanism and to estimate the equilibrium and kinetic parameters of the identified model) and of the ZLC method (the potential to derive direct information about the processes on the particle level, by eliminating the influence of the adsorber). The frequency response functions of a ZLC system, up to the third order, and for three simple kinetic mechanisms (film resistance control, micropore diffusion control and pore-surface diffusion control) are derived and simulated. The procedure for estimation of the equilibrium and kinetic parameters is defined and illustrated based on numerical simulations. Nomenclature A input amplitudẽ a c first order coefficient of the Taylor series expansion of the isotherm relation q = ϕ(c) a q first order coefficient of the Taylor series expansion of the isotherm relation c = (q) B amplitude of the output harmonic b c second order coefficient of the Taylor series expansion of the isotherm relation q = ϕ(c) M. Petkovska ( ) q second order coefficient of the Taylor series expansion of the isotherm relation c = (q) C concentration in the fluid phase, mol/m 3 C i concentration in the fluid phase within the particle pores (pore-surface diffusion model), mol/m 3 c nondimensional concentration in the fluid phase c i nondimensional concentration in the fluid phase within the particle pores (pore-surface diffusion model) c c third order coefficient of the Taylor series expansion of the isotherm relation q = ϕ(c) c qthird order coefficient of the Taylor series expansion of the isotherm relation c = (q) D eff effective diffusion coefficient, m 2 /s D p pore diffusion coefficient, m 2 /s D s surface diffusion coefficient, m 2 /s D μ micropore diffusion coefficient, m 2 /s F FRF on the particle level G FRF on the column level k m mass transfer coefficient, 1/s Q concentration in the adsorbent particle, mol/m 3 q nondimensional concentration in the adsorbent particle Q i concentration in the solid phase (pore-surface diffusion model), mol/m 3 q i nondimensional concentration in the solid phase (pore-surface diffusion model) R particle half-dimension, m R μ microparticle half-dimension, m r particle spatial coordinate, m r μ microparticle spatial coordinate, m t time, s V volume of the ZLC bed, m 3 V volumetric flow-rate, m 3 /s W function defined in (49) 224 Adsorption (2008) 14: 223-239