Adsorption of Anionic and Cationic Dyes on Activated Carbon Prepared from Oak Cupules: Kinetics and Thermodynamics Studies
Abstract
:1. Introduction
2. Experimental
2.1. Preparation of the Adsorbate Solutions
2.2. Preparation of the Activated Charcoal
2.3. Characterizations of the Activated Charcoal
2.4. Batch Adsorption Experiments
2.5. Isotherm and Kinetic Studies
2.6. Adsorption Thermodynamic
3. Results and Discussion
3.1. Characterization of Adsorbate
3.2. Parametric Study of the Adsorption Process
3.2.1. Effect of Contact Time
3.2.2. Effect of ACOC Dose
3.2.3. Effect of Dye Concentration
3.2.4. Effect of pH
3.2.5. Effect of Temperature
3.3. Isotherm Studies
3.4. Kinetics Study
3.5. Thermodynamics
4. Reusability of ACOC
5. Conclusions
Author Contributions
Funding
Institutional Review Board Statement
Informed Consent Statement
Data Availability Statement
Acknowledgments
Conflicts of Interest
References
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Model | Name | Nonlinear Equation | Linear Equation | Parameters |
---|---|---|---|---|
Isotherm | Langmuir | Ce: Concentration of dye at equilibrium (mg L−1) qe: Amount of adsorbate adsorbed per unit mass of adsorbent at equilibrium (mg g−1) qm: Theoretical maximum adsorption capacity (mg g−1) kl: Langmuir constant related to the rate of adsorption 1/n and KF: Freundlich constants kt: Temkin constant | ||
Freundlich | ||||
Temkin | ||||
Kinetics | Pseudo-first order | qt: Amount of adsorbate adsorbed per unit mass of adsorbent at time t constant (mg g−1) k1p: Pseudo-first order rate constant k2: Second order rate constant k2p: Second order rate constant kint: Intraparticle diffusion rate constant | ||
Second order | ||||
Pseudo-second order | ||||
Intraparticle diffusion |
Model | Parameter | NBB | CV |
---|---|---|---|
Langmuir | qm (mg g−1) | 213 | 625 |
kl | 0.2814 | 0.2462 | |
R2 | 0.992 | 0.935 | |
Freundlich | 1/n | 0.1585 | 0.2572 |
Kf | 106.9 | 227 | |
R2 | 0.9768 | 0.9164 | |
Temkin | qm (mg g−1) | 25.5 | 103.5 |
kT | 46.0 | 6.41 | |
R2 | 0.9570 | 0.8475 |
Model | Parameter | NBB | CV |
---|---|---|---|
Pseudo-first order | K1p | 0.0173 | 0.0202 |
qe | 125 | 66.3 | |
R2 | 0.9917 | R2 = 0.9439 | |
Second order | k2 | −(4 × 10−5) | −(2 × 10−6) |
qe | 91.7 | 294 | |
R2 | 0.571 | 0.4997 | |
Pseudo-second order | k2p | 3.08 × 10−5 | 8.35 × 10−4 |
qe | 278 | 333 | |
R2 | R2 = 0.5981 | R2 = 1 | |
Intraparticle diffusion | kint | 0.0861 | 6.6788 |
R2 | 0.9469 | 0.7128 |
Dye | ΔH (KJ/mol) | ΔS (J/mol) | ΔG (KJ/mol) | ||
---|---|---|---|---|---|
303 K | 308 K | 313 K | |||
NBB | 37.15 | 137.99 | −4.68 | −5.37 | −6.06 |
CV | 60.75 | 223.75 | −11.42 | −12.61 | −13.80 |
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Alkhabbas, M.; Al-Ma’abreh, A.M.; Edris, G.; Saleh, T.; Alhmood, H. Adsorption of Anionic and Cationic Dyes on Activated Carbon Prepared from Oak Cupules: Kinetics and Thermodynamics Studies. Int. J. Environ. Res. Public Health 2023, 20, 3280. https://doi.org/10.3390/ijerph20043280
Alkhabbas M, Al-Ma’abreh AM, Edris G, Saleh T, Alhmood H. Adsorption of Anionic and Cationic Dyes on Activated Carbon Prepared from Oak Cupules: Kinetics and Thermodynamics Studies. International Journal of Environmental Research and Public Health. 2023; 20(4):3280. https://doi.org/10.3390/ijerph20043280
Chicago/Turabian StyleAlkhabbas, Manal, Alaa M. Al-Ma’abreh, Gada Edris, Tasneem Saleh, and Heba Alhmood. 2023. "Adsorption of Anionic and Cationic Dyes on Activated Carbon Prepared from Oak Cupules: Kinetics and Thermodynamics Studies" International Journal of Environmental Research and Public Health 20, no. 4: 3280. https://doi.org/10.3390/ijerph20043280