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. 2020 Jan 15;18(1):35-50.
doi: 10.1007/s40201-019-00435-1. eCollection 2020 Jun.

Microwave assist sorption of crystal violet and Congo red dyes onto amphoteric sorbent based on upcycled Sepia shells

Affiliations

Microwave assist sorption of crystal violet and Congo red dyes onto amphoteric sorbent based on upcycled Sepia shells

K Z Elwakeel et al. J Environ Health Sci Eng. .

Abstract

A new sorbent based on Sepia shells (cuttlefish bones) has been synthesized (SSBC) and tested for the sorption of cationic dye (crystal violet, CV) and an anionic dye (congo red, CR). SSBC was produced by reaction of sepia shells powder with urea in the presence of formaldehyde. In the first part of the work, the sorbent was characterized using scanning electron microscopy, energy dispersive X-ray analysis, Fourier-transform infra-red spectrometry and titration (for determining pHPZC). In a second step, sorption properties were tested on the two dyes through the study of pH effect, sorbent dosage, temperature and ionic strength; the sorption isotherms and uptake kinetics were analyzed at the optimum pH: Langmuir equation fits isotherm profiles while the kinetic profile can be described by the pseudo-second order rate equation. Maximum sorption capacities reach up to 0.536 mmol g-1 for CV and 0.359 mmol g-1 for CR, at pH 10.6 and 2.4, respectively. The comparison of sorption properties at different temperatures shows that the sorption is endothermic. Processing to the sorption under microwave irradiation (microwaved enforced sorption, MES) increases mass transfer and a contact time as low as 1 min is sufficient under optimized conditions (exposure time and power) reaching the equilibrium, while 2-3 h were necessary for "simple" sorption. Dye desorption was successfully tested using 0.5 M solutions of NaOH and HCl for the removal of CR and CV, respectively. The sorbent can be re-used for a minimum of four cycles of sorption/desorption. Finally, the sorbent was successfully tested on spiked tap water and real industrial wastewater.

Keywords: Industrial wastewater; Microwave enforced sorption; Sepia shells functionalization; Sorbent recycling; Sorption.

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Conflict of interest statement

Conflict of interestThe authors confirm that there are no known conflicts of interest associated with this publication and there has been no significant financial support for this work that could have influenced its outcome.

Figures

Fig. 1
Fig. 1
pH effect on CV and CR dyes sorption onto SSBC; (T: 25 ± 1 °C; C0: 20 mg L−1; sorbent mass 1.5 g L−1)
Fig. 2
Fig. 2
Graph of ∆pH (pHeq – pH0) against initial pH (pH0) from CV and CR sorption
Fig. 3
Fig. 3
Uptake kinetics of (a) CV dye (b) CR dye sorption onto SSBC (C0: 20 mg L−1; T: 25 ± 1 °C; volume: 200 mL; sorbent mass 0.3 g) at normal sorption
Fig. 4
Fig. 4
Uptake kinetics of (a) CV dye (b) CR dye sorption onto SSBC (C0: 20 mg L−1; T: 25 ± 1 °C; volume: 20 mL; sorbent mass 0.03 g) at microwave enforced sorption
Fig. 5
Fig. 5
Effect of dyes concentrations on the sorption process for (a) CV dye, (b) CR dye, (sorption time 90 min, sorbent dosage 1.5 g L−1 and at 20 °C)
Fig. 6
Fig. 6
van’t Hoff plots for CV and CR dyes sorption
Fig. 7
Fig. 7
Effect of different microwave power intensities on CV and CR removal % (C0: 20 mg L−1; T: 25 ± 1 °C; volume; 20 mL; sorbent mass: 0.03 g)
Fig. 8
Fig. 8
Removal (%) of SSBC towards CV and CR dyes from different concentrations of spiked water samples for (a) CV dye, (b) CR dye, (sorption time 90 min, sorbent dosage 1.5 g L−1 and at 20 °C)

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