Freundlich equation

Freundlich's original data for adsorption of acetic acid (page 392 in [3]) and a fit according to Freundlich's exponential law

The Freundlich adsorption isotherm is mathematically expressed as

${\displaystyle {\frac {x}{m}}=Kp^{1/n}}$

It is also written as

${\displaystyle \log {\frac {x}{m}}=\log K+{\frac {1}{n}}\log p}$

or

${\displaystyle {\frac {x}{m}}=Kc^{1/n}}$

It is also written as

${\displaystyle \log {\frac {x}{m}}=\log K+{\frac {1}{n}}\log c}$

where

x = mass of adsorbate

m = mass of adsorbent

p = Equilibrium pressure of adsorbate

c = Equilibrium concentration of adsorbate in solution.

K and n are constants for a given adsorbate and adsorbent at a particular temperature.

At high pressure 1/n = 0, hence extent of adsorption becomes independent of pressure.

It is used in cases where the actual identity of the solute is not known, such as adsorption of colored material from sugar, vegetable oil etc.

The Freundlich equation is unique; consequently, if the data fit the equation, it is only likely, but not proved, that the surface is heterogeneous. The heterogeneity of the surface can be confirmed with calorimetery. Homogeneous surfaces (or heterogeneous surfaces that exhibit homogeneous adsorption (single site)) have a constant ${\displaystyle \Delta H}$ of adsorption. On the other hand, heterogenous adsorption (multi-site) have a variable ${\displaystyle \Delta H}$ of adsorption depending on the percent of sites occupied. When the adsorbate pressure (or concentration) are low, high energy sites will be occupied; and as the pressure (or concentration) increases, the lesser energy sites will be occupied resulting in a lower ${\displaystyle \Delta H}$ of adsorption[4].

Experimentally it was determined that extent of gas adsorption varies directly with pressure, and then it directly varies with pressure raised to the power 1/n until saturation pressure P_s is reached. Beyond that point, the rate of adsorption saturates even after applying higher pressure. Thus, the Freundlich adsorption isotherm fails at higher pressure.

• Langmuir adsorption model

• Jaroniec, M. (1975). "Adsorption on heterogeneous surfaces: The exponential equation for the overall adsorption isotherm". Surface Science. 50 (2): 553–564. Bibcode:1975SurSc..50..553J. doi:10.1016/0039-6028(75)90044-8.
• Levan, M. Douglas; Vermeulen, Theodore (1981). "LeVan, M. Douglas, and Theodore Vermeulen. "Binary Langmuir and Freundlich isotherms for ideal adsorbed solutions." The Journal of Physical Chemistry 85.22 (1981): 3247-3250". The Journal of Physical Chemistry. 85 (22): 3247–3250. doi:10.1021/j150622a009.
• "Freundlich Equation". Archived from the original on 3 March 2016.

• "Freundlich equation solver".
• "Freundlich Adsorption Isotherm". Archived from the original on 2 March 2012.