Figures & data
Figure 3. The X-ray diffraction (XRD) patterns of the MgO products synthesized using citric acid as a fuel and subjected to calcination at 800 °C.
![Figure 3. The X-ray diffraction (XRD) patterns of the MgO products synthesized using citric acid as a fuel and subjected to calcination at 800 °C.](/cms/asset/69a1633c-1919-46bd-bef1-14d4971ea968/tabs_a_2375663_f0003_c.jpg)
Figure 4. The FT-IR spectra of the MgO nanostructures that were produced and subsequently calcined at 800 °C, using citric acid (a) diclofenac sodium (b) MgO and (c) MgO and diclofenac sodium.
![Figure 4. The FT-IR spectra of the MgO nanostructures that were produced and subsequently calcined at 800 °C, using citric acid (a) diclofenac sodium (b) MgO and (c) MgO and diclofenac sodium.](/cms/asset/1b82b1ac-3338-4741-891d-128c163759e3/tabs_a_2375663_f0004_c.jpg)
Figure 5. DCF and Cd2+ removal efficiency from aqueous solution using B-nZVI composite (●), activated charcoal (▲), MgO (■) versus time, adsorbent dose 0.1 g, C0100 mg L−1, pH 7, and T = 25 °C.
![Figure 5. DCF and Cd2+ removal efficiency from aqueous solution using B-nZVI composite (●), activated charcoal (▲), MgO (■) versus time, adsorbent dose 0.1 g, C0100 mg L−1, pH 7, and T = 25 °C.](/cms/asset/6bacd3a7-a3ec-40b7-ae21-8c6724c1796c/tabs_a_2375663_f0005_c.jpg)
Figure 7. Variables influencing the adsorption efficiency of DCF at a concentration of 100 mg L−1 and Cd2+: MgO nanoparticles dosage at 25 °C and pH 7.
![Figure 7. Variables influencing the adsorption efficiency of DCF at a concentration of 100 mg L−1 and Cd2+: MgO nanoparticles dosage at 25 °C and pH 7.](/cms/asset/a129656e-f6bf-45db-8810-61868902e94a/tabs_a_2375663_f0007_c.jpg)
Figure 8. The effect of DCF and Cd2+ initial concentration on the removal efficiency using MgO nanoparticles.
![Figure 8. The effect of DCF and Cd2+ initial concentration on the removal efficiency using MgO nanoparticles.](/cms/asset/0f081c1b-83dc-4f72-94ef-3f588edc46be/tabs_a_2375663_f0008_c.jpg)
Figure 9. Plotting the pseudo-second-order kinetic parameters for the removal of DCF and Cd2+ by MgO. (●) DCF and Cd2+ (■).
![Figure 9. Plotting the pseudo-second-order kinetic parameters for the removal of DCF and Cd2+ by MgO. (●) DCF and Cd2+ (■).](/cms/asset/ebac1bad-b75e-45c0-9581-85e9d3498fa9/tabs_a_2375663_f0009_c.jpg)
Table 1. The Langmuir isotherm model was utilized to obtain values of K, qmax, and the coefficient of determination (R2) for the removal of both DCF and Cd2+ using the B-nZVI composite at 25 °C.
Figure 10. Linear graphs representing the Langmuir isotherm model for the adsorption of DCF and Cd2+ using MgO nanoparticles and the B-nZVI composite at of 298 K, respectively.
![Figure 10. Linear graphs representing the Langmuir isotherm model for the adsorption of DCF and Cd2+ using MgO nanoparticles and the B-nZVI composite at of 298 K, respectively.](/cms/asset/cdbc6326-77d9-455c-85eb-1bcdedd97ed9/tabs_a_2375663_f0010_c.jpg)
Figure 11. Influence of temperature on the percentage removal of diclofenac sodium and Cd2+ at pH = 7, C0=25mg L−1, adsorbent dose = 0.1 g and time = 3h.
![Figure 11. Influence of temperature on the percentage removal of diclofenac sodium and Cd2+ at pH = 7, C0=25mg L−1, adsorbent dose = 0.1 g and time = 3h.](/cms/asset/47a72da6-69b9-4128-89f1-7f6644e4c83f/tabs_a_2375663_f0011_b.jpg)
Table 2. The thermodynamic parameters determined at various concentrations.
Table 3. The filtration procedure involved the passage of 1 liter of pure water solutions containing DCF and Cd2+ at concentrations of 100, 10, 1.0 and 0.01 mg.L−1 through laboratory filters.
Table 4. Antibacterial activity of Cd2+, DCF, MgO, MgO + DCF, MgO + Cd2+, MgO + Cd2+ + DCF, levo the positive control to gram-positive bacteria and the negative control (water) in relation to the inhibition zone using the agar well diffusion method.