In this context, an analysis of the thermodynamics of water sorption is presented and a multilayer heat of sorption equation is derived within the framework of the Guggenheim Anderson deBoer (GAB) model.
Selective sorption is also named as specific or non-exchangeable sorption, while non-selective sorption is named as exchangeable sorption.
Sorption is used for absorption/adsorption heat pumps (sorption refrigeration) and sorption for thermal energy storage (TES).
Recent work has shown sorption is pH dependent and that as available sorption sites approach saturation, phosphorus transport through groundwater may occur (Domagalski and Johnson 2011).
Iodine sorption is mostly reversible, but a small fraction is not.
The Freundlich relation describes multilayer sorption and can be stated as Eq. (4): ln q e = ln k f + 1 n ln c e (4 where kf and n are the Freundlich constants related to the adsorption capacity and intensity, respectively.
The sorption was temperature dependent.
(g) The sorption was temperature dependent.
Hence, Naph sorption was suppressed.
After a reaction time of 48 h, Ni sorption and Zn sorption are nearly complete.
