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. 2021 Mar 11;11(1):5686.
doi: 10.1038/s41598-021-84797-3.

Synthesis and characterization of Cu(OH)2-NWs-PVA-AC Nano-composite and its use as an efficient adsorbent for removal of methylene blue

Affiliations

Synthesis and characterization of Cu(OH)2-NWs-PVA-AC Nano-composite and its use as an efficient adsorbent for removal of methylene blue

Sivarama Krishna Lakkaboyana et al. Sci Rep. .

Erratum in

Abstract

The present study focused on the synthesis of copper hydroxide nanowires decorated on activated carbon (Cu(OH)2-NWs-PVA-AC). The obtained Cu(OH)2-NWs-PVA-AC Nano-composite was distinguished by XRD, SEM, EDX, BET, FTIR and XPS respectively. Besides, different variables such as solution pH, and initial dye concentration, contact time, and temperature were performed on the adsorption efficiency of MB in a small batch reactor. Further, the experimental results are analyzed by various kinetic models via PFO, PSO, intra-particle diffusion and Elovich models, and the results revealed that among the kinetic models, PSO shows more suitability. In addition, different adsorption isotherms were applied to the obtained experimental data and found that Langmuir-Freundlich and Langmuir isotherm were best fits with the maximum adsorption capacity of 139.9 and 107.6 mg/g, respectively. The Nano-composite has outstanding MB removal efficiency of 94-98.5% with a span of 10 min. and decent adsorption of about 98.5% at a pH of 10. Thermodynamic constants like Gibbs free energy, entropy, and enthalpy were analyzed from the temperature reliance. The results reveal the adsorption processes are spontaneous and exothermic in nature. The high negative value of ΔG° (- 44.11 to - 48.86 kJ/mol) and a low negative value of ΔH° (- 28.96 kJ/mol) show the feasibility and exothermic nature of the adsorption process. The synthesized dye was found to be an efficient adsorbent for the potential removal of cationic dye (methylene blue) from wastewater within a short time.

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Conflict of interest statement

The authors declare no competing interests.

Figures

Figure 1
Figure 1
XRD patterns of Cu(OH)2-NWs, and Cu(OH)2-NWs-PVA-AC Nano-composite.
Figure 2
Figure 2
SEM images of (a) Cu(OH)2-NWs, and (b) Cu(OH)2-NWs-PVA-AC Nano-composite.
Figure 3
Figure 3
(a) SEM–EDS spectra of the Cu(OH)2-NWs, (b) SEM–EDS spectra of the Cu(OH)2-NWs-PVA-AC Nano-composite.
Figure 4
Figure 4
(a) N2 adsorption/desorption isotherms. (b) Pore size distribution and pore volume of raw Cu(OH)2-NWs-PVA-AC.
Figure 5
Figure 5
FTIR patterns of Cu(OH)2-NWs, and Cu(OH)2-NWs-PVA-AC Nano-composite.
Figure 6
Figure 6
Effect of pH. Conditions: MB concentration: 50 mg/L; Volume = 25 mL, Absorbent dose = 30 mg; Temp. = 30 ± 10 °C; Speed of agitation = 200 rpm; Contact time = 60 min.
Figure 7
Figure 7
Effect of dye concentration and contact time on MB. Conditions: MB concentration: 10, 20 and 30 mg/L; Volume = 25 mL, Absorbent dose = 30 mg; Temp. = 30 ± 10 °C; Speed of agitation = 200 rpm; Contact time = 60 min.
Figure 8
Figure 8
Pseudo-first-order, Pseudo-second-order, and Elovich, models kinetics plots for different concentration: (a) 10 mg/L, (b) 20 mg/L, (c) 30 mg/L. Conditions: As shown in Fig. 7.
Figure 9
Figure 9
Adsorption Intraparticle diffusion model for adsorption of MB onto Cu(OH)2-NWs-PVA-AC Nano-composite. Conditions: As shown in Fig. 7.
Figure 10
Figure 10
Langmuir, Freundlich, Langmuir–Freundlich, Temkin, and Redlich adsorption isotherms at different temperatures (a) 35 °C, (b) 45 °C and (c) 55 °C) for the adsorption of MB onto Cu(OH)2-NWs-PVA-AC Nano-composite. Conditions: MB concentration: 60, 80 and 100 mg/L; Volume = 25 mL, Absorbent dose = 30 mg; Temp. = 35, 45, and 55 °C; Speed of agitation = 200 rpm; Contact time = 60 min.
Figure 11
Figure 11
Thermodynamic parameter for MB adsorption onto Cu(OH)2-NWs-PVA-AC Nano-composite. Conditions: As shown in Fig. 10.
Figure 12
Figure 12
Desorption of MB onto Cu (OH)2-NWs-PVA-AC.

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