Micropollutant removal in real WW by photo-Fenton (circumneutral and acid pH) with BLB and LED lamps

dc.contributor.author
López Vinent, Núria
dc.contributor.author
Cruz Alcalde, Alberto
dc.contributor.author
Gutiérrez, C.
dc.contributor.author
Marco Buj, Pilar
dc.contributor.author
Giménez Farreras, Jaume
dc.contributor.author
Esplugas Vidal, Santiago
dc.date.issued
2022-05-13T16:47:05Z
dc.date.issued
2022-05-13T16:47:05Z
dc.date.issued
2020-01-01
dc.date.issued
2022-05-13T16:47:05Z
dc.identifier
1385-8947
dc.identifier
https://hdl.handle.net/2445/185600
dc.identifier
695586
dc.description.abstract
In this study, photo-Fenton treatment was performed to remove a target compound (propranolol, PROP) from wastewaters of secondary effluents coming from WWTP. Two different radiation sources were tested: BLB and UV-A LEDs, which implies low electrical power and no mercury content. The differences observed in the PROP removal with both lamps may be due to the different radiation distribution, absorption inside the reactor, emission angle and wavelength emission, which are key parameters in the radiation field of the photoreactor. Four wastewaters (IFAS, MBR, CAS and CAS-NE) and ultrapure water were tested to determine the influence of water matrix. Instead the propranolol degradation using UV-A LEDs was smaller than using BLB lamps, in ultrapure water the degradation was very similar. The matrices with more organic matter and turbidity achieved low propranolol removals due to the competition for hydroxyl radicals and the effect of the light scattering. In addition, photo-Fenton at neutral pH (to avoid the acidification/basification) was also carried out using two chelating agents (EDDS and EDTA). Two molar ratios ligand-Fe(II) were tested (1:1 and 1.5:1). EDDS with L:Fe(II) molar ratio 1:1 was selected based on studies of MP degradation, biodegradability and toxicity. Comparisons between conventional photo-Fenton and photo-Fenton with EDDS-Fe(II) were performed with UV-A LEDs. For Milli-Q and IFAS best results were achieved in conventional photo-Fenton (32.9% for IFAS instead of 14.3% in EDDS-Fe(II)). Contrary, for the MBR, CAS and CAS-NE the best results were shown for EDDS-Fe(II) photo-Fenton. In IFAS, biopolymers and humic substances were the responsible of the different behavior of IFAS than other WW. Finally, for conventional photo-Fenton, dark Fenton plays an important role during the first 30 s, then, photo-Fenton controls the process. For circumneutral photo-Fenton, dark Fenton is not so important during the initial time. These observations have been corroborated by different kinetic fittings for different reaction times.
dc.format
application/pdf
dc.language
eng
dc.publisher
Elsevier B.V.
dc.relation
Versió postprint del document publicat a: https://doi.org/10.1016/j.cej.2019.122416
dc.relation
Chemical Engineering Journal, 2020, vol. 379
dc.relation
https://doi.org/10.1016/j.cej.2019.122416
dc.rights
cc-by-nc-nd (c) Elsevier B.V., 2020
dc.rights
https://creativecommons.org/licenses/by-nc-nd/4.0/
dc.rights
info:eu-repo/semantics/openAccess
dc.source
Articles publicats en revistes (Enginyeria Química i Química Analítica)
dc.subject
Díodes electroluminescents
dc.subject
Quelants
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Contaminants
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Light emitting diodes
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Chelating agents
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Pollutants
dc.title
Micropollutant removal in real WW by photo-Fenton (circumneutral and acid pH) with BLB and LED lamps
dc.type
info:eu-repo/semantics/article
dc.type
info:eu-repo/semantics/acceptedVersion


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