| Autor: |
Sarran, Mohammed A., AbdulRazak, Adnan A., Abid, Mohammed F., Jawad Al-Bayati, Alaa Dhari, Rashid, Khalid T., Shehab, Mohammed Ahmed, Mohammed, Haidar Hasan, Alsarayefi, Saad, Alhafadhi, Mahmood, Alktranee, Mohammed |
| Předmět: |
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| Zdroj: |
ChemEngineering; Oct2024, Vol. 8 Issue 5, p92, 18p |
| Abstrakt: |
Oily wastewater is a major environmental issue resulting from different industrial and manufacturing activities. Contaminated water with oil represents a significant environmental hazard that can harm numerous life forms. Several methodologies have been tested for the removal of oily wastewater from aqueous solutions, and adsorption in a flow-through reactor is an effective mechanism to reduce these effluents. This study focuses on evaluating the ability of Fe3O4/Bent material to adsorb gasoline emulsion from a solution using a fixed-bed column, and it involves analyzing the resulting breakthrough curves. The FT-IR, SEM, EDX, and XRD techniques were used to characterize Fe3O4/Bent. Various ranges of variables were examined, including bed height (2–4 cm), flow rate (3–3.8 mL/min), and initial concentration (200–1000 mg/L), to determine their impacts on the mass transfer zone (MTZ) length and the adsorption capacity (qe). It was shown that a higher bed height and a lower flow rate contributed to a longer time of breakthrough and exhaustion. At the same time, it was noted that under high initial gasoline concentrations, the fixed-bed system rapidly reached breakthrough and exhaustion. Models like the Yoon–Nelson and Thomas kinetic column models were employed to predict the breakthrough curves. Thomas and Yoon–Nelson's breakthrough models provided a good fit for the breakthrough curves with a correlation coefficient of R2 > 0.95. Furthermore, with a fixed-bed system, the Thomas and Yoon–Nelson models best describe the breakthrough curves for gasoline removal. [ABSTRACT FROM AUTHOR] |
| Databáze: |
Complementary Index |
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