An adsorption equilibrium model was developed for predicting the total orga
nic carbon (TOC) removal by the International Space Station water processor
's multifiltration beds. Ideal adsorbed solution theory is used to describe
the competitive interactions between fictive components (FCs) that make up
the TOC, The FC physical properties were based on several identified compo
unds to represent the distribution adsorbing compounds in the wastewaters.
The TOC isotherms were performed using the wastewaters on three absorbents
(a coconut-based granular activated carbon, a coal-based granular activated
carbon, and a polymeric-based resin), which are contained in the multifilt
ration beds. The isotherms were used to validate the model for all three ad
sorbents. The FCs were determined in such a way that they can describe the
TOC concentration for multiple beds in series.