Abstract
Two types of adsorbents were used to treat oily wastewater, activated carbon and zeolite. The
removal efficiencies of these materials were compared to each other. The results showed that
activated carbon performed some better properties in removal of oil. The experimental methods
which were employed in this investigation included batch and column studies. The former was used
to evaluate the rate and equilibrium of carbon and zeolie adsorption, while the latter was used to
determine treatment efficiencies and performance characteristics. Expanded bed adsorber was
constructed in the column studies. In this study, the adsorption behavior of vegetable oil (corn oil)
onto activated carbon and zeolite was examined as a function of the concentration of the adsorbate,
contact time, adsorbent dosage and amount of coagulant salt(calcium sulphate) added . The
adsorption data was modeled with Freundlich and Langmuir adsorption isotherms. and it was found
that the adsorption process on activated carbon and zeolite fit the Freundlich isotherm model. The
amount of oil adsorbed increased with increasing the contact time, but longer mixing duration did
not increase residual oil removal from wastewater due to the coverage of the adsorbent surface with
oil molecules. It was found that as the dosage of adsorbent increased, the percentage of residual oil
removal also increased. The effects of adsorbent type and amount of coagulant salt(calcium
sulphate) added on the breakthrough curve were studied in details in the column studies. Expanded
bed behavior was modeled using the Richardson-Zaki correlation between the superficial velocity of the feed
stream and the void fraction of the bed at moderate Reynolds number.
removal efficiencies of these materials were compared to each other. The results showed that
activated carbon performed some better properties in removal of oil. The experimental methods
which were employed in this investigation included batch and column studies. The former was used
to evaluate the rate and equilibrium of carbon and zeolie adsorption, while the latter was used to
determine treatment efficiencies and performance characteristics. Expanded bed adsorber was
constructed in the column studies. In this study, the adsorption behavior of vegetable oil (corn oil)
onto activated carbon and zeolite was examined as a function of the concentration of the adsorbate,
contact time, adsorbent dosage and amount of coagulant salt(calcium sulphate) added . The
adsorption data was modeled with Freundlich and Langmuir adsorption isotherms. and it was found
that the adsorption process on activated carbon and zeolite fit the Freundlich isotherm model. The
amount of oil adsorbed increased with increasing the contact time, but longer mixing duration did
not increase residual oil removal from wastewater due to the coverage of the adsorbent surface with
oil molecules. It was found that as the dosage of adsorbent increased, the percentage of residual oil
removal also increased. The effects of adsorbent type and amount of coagulant salt(calcium
sulphate) added on the breakthrough curve were studied in details in the column studies. Expanded
bed behavior was modeled using the Richardson-Zaki correlation between the superficial velocity of the feed
stream and the void fraction of the bed at moderate Reynolds number.
Keywords
activated carbon.
Oil removal; adsorption; expanded beds; wastewater treatment; zeolite