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Degradation of hydroxychloroquine in aqueous solutions under electron beam treatment Cover

Degradation of hydroxychloroquine in aqueous solutions under electron beam treatment

Open Access
|Jun 2024

Figures & Tables

Fig. 1.

Dégradation of 2.88 × 10-4 M of hydroxychloroquine under electron beam treatment. (a) UV-VIS absorption spectrum of HCQ solution with an initial concentration of 2.88 × 10—4 M was observed at 343 nm at doses ranging from 0 kGy to 7 kGy. (b) The removal efficiency of 2.88 × 10-4 M HCQ solution under EB irradiation.
Dégradation of 2.88 × 10-4 M of hydroxychloroquine under electron beam treatment. (a) UV-VIS absorption spectrum of HCQ solution with an initial concentration of 2.88 × 10—4 M was observed at 343 nm at doses ranging from 0 kGy to 7 kGy. (b) The removal efficiency of 2.88 × 10-4 M HCQ solution under EB irradiation.

Fig. 2.

Degradation of different concentrations of hydroxychloroquine solutions under EB irradiation. (a) Variation in the removal efficiency with increasing HCQ concentration. (b) Variation of reaction rate k with increasing concentrations of HCQ. (c) Variation of reaction rate k with increasing doses for different concentrations of HCQ.
Degradation of different concentrations of hydroxychloroquine solutions under EB irradiation. (a) Variation in the removal efficiency with increasing HCQ concentration. (b) Variation of reaction rate k with increasing concentrations of HCQ. (c) Variation of reaction rate k with increasing doses for different concentrations of HCQ.

Fig. 3.

The effect of pH on the removal of 2.88 × 10-4 M of hydroxychloroquine. (a) Removal efficiency under different initial pH under electron beam treatment. (b) The changes in pH during electron beam irradiation with different initial pH.
The effect of pH on the removal of 2.88 × 10-4 M of hydroxychloroquine. (a) Removal efficiency under different initial pH under electron beam treatment. (b) The changes in pH during electron beam irradiation with different initial pH.

Fig. 4.

Changes in pH concentration during electron beam treatment of 2.88 × 10-4 M HCQ. The pH varied from slightly acidic before irradiation to acidic at the end of irradiation.
Changes in pH concentration during electron beam treatment of 2.88 × 10-4 M HCQ. The pH varied from slightly acidic before irradiation to acidic at the end of irradiation.

Fig. 5.

Release of the Cl- ion during the degradation of 2.88 × 10-4 M solution of HCQ under electron beam treatment.
Release of the Cl- ion during the degradation of 2.88 × 10-4 M solution of HCQ under electron beam treatment.

Fig. 6.

(a) Nitrification of organic bound nitrogen (HCQ[N]) with subsequent formation of NO3− during the electron beam treatment of 2.88 × 10-4 M of HCQ. (b) Formation of NH4+ ion. HCQ, hydroxychloroquine; TKN, total Kjeldahl nitrogen; TN, total nitrogen.
(a) Nitrification of organic bound nitrogen (HCQ[N]) with subsequent formation of NO3− during the electron beam treatment of 2.88 × 10-4 M of HCQ. (b) Formation of NH4+ ion. HCQ, hydroxychloroquine; TKN, total Kjeldahl nitrogen; TN, total nitrogen.

Fig. 7.

Changes in the dissolved oxygen concentration during electron beam irradiation of 2.88 × 10-4 M HCQ.
Changes in the dissolved oxygen concentration during electron beam irradiation of 2.88 × 10-4 M HCQ.

Fig. 8.

Variation in COD and TOC during electron beam degradation of 2.88 × 10-4 M HCQ aqueous solutions.
Variation in COD and TOC during electron beam degradation of 2.88 × 10-4 M HCQ aqueous solutions.

Methods for the removal of hydroxyquinine from aqueous solutions

MethodConditionsEfficiencyRef.
Photochemical decompositionpH 3–10Half-lives of 5.5 min (pH3) to 23.1 h (pH4) Hydrolytic degradation <5%[7, 8]
Adsorbents
Living microalgaeHCQ 20 mg·L-1, pH 9.9, 45 min, 300 rpm stirring speed microalgae loading of 100 mg·L-192.10 ± 1.25% maximum biosorption capacity is 339.02 mg·g-1[18]
H3PO4-activated Cystoseira barbata (Stackhouse) C. Agardh biocharAdsorbent dose (0.025–1 g·L-1), pH (4–11) contact time (0–240 min) HCQ (10–50 mg·L-1)98.9% (qmax = 353.58 mg·g-1) surface area (1088.806 m2·g-1)[19]
Natural zeolite CPpH 2–7.5 298 K, 303 K, and 308 K7 mg·g-1 7 cycles reuse[20]
Algerian kaolin0.05–0.15 g·L-1 sorbent, and pH of 3–7 5–50 mg·L-1 HCQCapacity of 51 mg·g-1 0.15 g·L-1 of kaolin, 5 mg·L-1 as HCQ initial concentration, and pH 7 are optimal[21]
Catalysis
ZnO-CP catalyst2 g·L-1 15% ZnO-CP pH = 7.5 UV-A radiation, 10 mg·L-1 HCQ, 180 min96%[17]
Modified titanium oxide using beta-bismuth oxide TiO2/ß-Bi2O3120 min, pH 3–11 10 mg·L-1 HCQ, 0.1 g·L-1 catalyst, 0.1 mg·L-1 H2O291.8% 6 cycles >70% degradation[12]
MoS2/CNTs nanocompositeMoS2/CNTs 10:1 ratio loading of 0.1 g·L-1 pH of 8.7, HCQ-20 mg·L-1 120 min70% Lower band gap energy (1.2 eV), higher specific surface area (30.6 m2·g-1)[13]
Ti3GeC2 with peroxydisulfate20 mg·L-1 HCQ 0.2 g·L-1 Ti3GeC2, 0.15 mmol·L-1 PDS, ultrasound irradiation 80 min60.42% Dependent on catalyst dosage (0.1–0.2 g·L-1)[16]
Advanced oxidation processess
Electrochemical oxidationBDD anodes, HCQ 36–250 mg·L-1, j = 20 mA·cm-2, pH = 7.1, T = 25°C, 0.05 M Na2SO4100%[14]
Electrochemical oxidationBDD electrode 15 mA·cm-2, 30 mA·cm-2, and 45 mA·cm-2100% COD (68%, 71%, and 84%)[15]
Fe(0)/HSO5/UV systemHSO5 dose: 194.31 mg·L-1; Fe(0): 198.83 mg·L-1; pH = 2.02 and HCQ 296.41 mg·L-1 60 min98.95%[21]
Gamma irradiation100 ppm HCQ A dose rate of 26.31 Gy·min-1 pH = 6.298.5% TOC removal (8 kGy) complete mineralization[22]
Gamma irradiation20 ppm HCQ, 1 kGy dose 4.2 kGy1100%[23]

Reaction rates of aminoquinoline derivatives with hydroxyl radical and hydrated electrons

Reactive sppHydroxychloroquine [30]Chloroquine [31]Amodiaquine [32]
OH9.5 × 109 M-1·s-17.3 × 109 M-1·s-19.0 × 109 M-1·s-1
eaq2.0 × 109 M-1·s-14.8 × 1010 M-1·s-11.6 × 1010 M-1·s-1

Rate constant k for different concentrations of hydroxychloroquine and corresponding R2 values

Concentation (mg·L-1)k (kGy-1)R2
 751.12870.9974
1001.07060.9887
1250.89800.9443
DOI: https://doi.org/10.2478/nuka-2024-0009 | Journal eISSN: 1508-5791 | Journal ISSN: 0029-5922
Language: English
Page range: 65 - 74
Submitted on: Oct 5, 2023
Accepted on: Feb 16, 2024
Published on: Jun 25, 2024
Published by: Institute of Nuclear Chemistry and Technology
In partnership with: Paradigm Publishing Services
Publication frequency: 4 issues per year

© 2024 Stephen Kabasa, Yongxia Sun, Sylwester Bułka, Andrzej G. Chmielewski, published by Institute of Nuclear Chemistry and Technology
This work is licensed under the Creative Commons Attribution-NonCommercial-NoDerivatives 4.0 License.