ABSTRACT
The present study recommends the electrocoagulation (EC) technique as a possible-green option to the conventional process for the efficient removal of ibuprofen (IBU) from drinking water for the first time, investigating a thorough analysis by optimizing operational parameters and kinetics/isotherms models. Under the optimum conditions 63% of IBU was removed. The double-stage electrocoagulation resulted in the removal efficiency of 73.8%. The dynamic and equilibrium data followed first-order and Freundlich. The treatment cost of IBU removal by electrocoagulation would be 1.8 US $/m3. It is possible to consider the EC technique as the promising IBU removal method.
Highlights
Ibuprofen removal was studied by electrocoagulation process.
Under optimum conditions, maximum removal efficiency of 73.8% was attained.
Adsorption and precipitation were the dominant ibuprofen removal path.
Freundlich model was the most suitable one.
Nomenclature
Electrocoagulation | = | EC |
Ibuprofen | = | IBU |
Electrolyte volume | = |
|
Electrode area | = |
|
Mass transfer coefficient | = |
|
Reaction time | = | t (s) |
Fractional IBU | = | |
Constant parameters | = | α and y |
Double stage electrocoagulation process | = | DSEC |
Sips equilibrium | = | KS |
Reaction rate constant | = | K1 |
RP exponent | = | β |
Redlich-Peterson | = | RP |
RP constants | = |
|
Freundlich constant | = |
|
Maximum adsorption | = | capacity Qm |
Vieth–Sladek constants | = | Kvs and Bvs |
Langmuir-Freundlich | = | LF |
Langmuir-Freundlich maximum adsorption capacity | = | qMLF (mg/g) |
Equilibrium constant for a heterogeneous solid | = | KLF |
Heterogeneous parameter | = | MLF |
Costs regarding operation | = | Cop |
Costs regarding energy | = | Cen, |
Costs regarding electrodes | = | Cel |
Declaration of interests
The authors declare that they have no known competing interests or personal relationships that could have appeared to influence the work reported in this paper.
Supplementary Material
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