Abstract
This work involves the treatment of simulated industrial waste water containing acid dye-stuffs with granular activated carbon adsorption selected as the treatment method. Predicting the rate at which adsorption takes place for a given system is probably the single most important factor for adsorber design, with adsorbate residence time and ultimately the reactor dimensions controlled by the system's kinetics. A fixed volume stirred tank reactor was used to study the kinetics of adsorption in a single component system. Process parameters including the rate of agitation, dye concentration and phase ratio were studied with results being modelled using a dual resistance external mass transfer and solid diffusivity model. A single value of solid diffusivity described the adsorption decay curves in most instances and also indicated that chemisorption is the likely process of acid dye adsorption onto activated carbon.
| Original language | English |
|---|---|
| Pages (from-to) | 1895-1899 |
| Number of pages | 5 |
| Journal | Water Research |
| Volume | 33 |
| Issue number | 8 |
| DOIs | |
| Publication status | Published - Jun 1999 |
| Externally published | Yes |
Keywords
- Activated carbon
- Adsorption
- Dyes
- External mass transfer
- Solid diffusion
- Stirred tank reactor