Physical Chemistry And Thermodynamics Codexery

Freundlich equation

Empirical isotherm relating adsorbed quantity to pressure or concentration.

Freundlich equation

The Freundlich equation, or Freundlich adsorption isotherm, is an empirical relationship that describes how much of a gas is adsorbed onto a solid surface as a function of gas pressure, and it also applies to the adsorption of a solute from a liquid phase onto a solid surface as a function of the solute's concentration. Herbert Freundlich introduced this expression in 1909 to represent the isothermal variation of adsorption. In his original experiments, Freundlich studied the adsorption of organic acids from aqueous solutions onto coal, using the ratio of the adsorbed mass of the adsorbate to the mass of the adsorbent (coal) as a key variable. The equation is mathematically expressed with constants specific to a given adsorbate and adsorbent at a fixed temperature. While the relationship is entirely empirical, it can also be derived non-empirically by considering that the equilibrium constant of the binding process changes due to surface heterogeneity and variations in the heat of adsorption. A limitation of the Freundlich isotherm is that it fails at higher pressures; experimentally, adsorption initially varies directly with pressure, then with pressure raised to a power, but eventually saturates and becomes independent of pressure. Because the equation is unique, data fitting it suggests, but does not prove, surface heterogeneity. Heterogeneity can be confirmed through calorimetry, as homogeneous surfaces have a constant heat of adsorption, whereas heterogeneous surfaces exhibit a variable heat of adsorption depending on site occupancy. At low pressure or concentration, high-energy sites are occupied first, followed by low-energy sites as pressure increases, leading to weaker adsorption.

field
Physical chemistry, surface science
known_for
Freundlich adsorption isotherm
year_formulated
1909
type
Empirical equation

Lore & Background

Herbert Freundlich introduced this empirical adsorption isotherm in 1909 to describe the relationship between the quantity of gas adsorbed per unit mass of a solid adsorbent and the gas pressure, under constant temperature. The same mathematical form applies to the adsorption of a solute from a liquid phase onto a solid, where the solute concentration replaces pressure. The equation is expressed as x/m = K c^(1/n), where x is the mass of adsorbate, m the mass of adsorbent, c the equilibrium concentration (or pressure for gases), and K and n are constants specific to the adsorbate, adsorbent, and temperature. The constant n is a correction factor, while K acts as a distribution coefficient. Although the equation is empirical, it can be derived theoretically by attributing the variation in the equilibrium constant to surface heterogeneity and a changing heat of adsorption. Freundlich’s original experiments involved the adsorption of three organic acids onto coal from aqueous solutions; he determined K and n values through numerical analysis. A key characteristic is that at high pressures, the extent of adsorption becomes independent of pressure. The equation is unique: if data fit it, heterogeneity of the surface is likely but not proven; calorimetry can confirm this. Homogeneous surfaces have a constant heat of adsorption, while heterogeneous surfaces show variable heat depending on site occupancy—high-energy sites fill first at low pressure, then low-energy sites at higher pressure, weakening the heat of adsorption. A major limitation is that the isotherm fails at high pressures, where adsorption saturates and no longer increases with pressure.

Reader's Guide

The Freundlich equation is mathematically expressed as x/m = K * c_eq^(1/n) or, in logarithmic form, log(x/m) = log K + (1/n) log c_eq. For gas-phase experiments, pressure p replaces concentration. The constants K and n are specific to a given adsorbate and adsorbent at a given temperature. The equation is unique in that if data fit it, it suggests but does not prove surface heterogeneity; calorimetry can confirm this. A limitation is that at higher pressures, the equation fails because adsorption saturates. When adsorption behavior can be properly fit by theoretically based isotherms (e.g., Langmuir or BET), those are usually preferred.

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