Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector

Phenol is a recalcitrant anthropogenic compound whose presence has been reported in both wastewater and drinking water; human exposure to phenolic substances can lead to health problems. The degradation of phenol (measured as COD decrease) through solar heterogeneous photocatalysis with immobilized...

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Main Authors: Felipe de J. Silerio-Vázquez, Cynthia M. Núñez-Núñez, María T. Alarcón-Herrera, José B. Proal-Nájera
Format: Article
Language:English
Published: MDPI AG 2022-05-01
Series:Catalysts
Subjects:
Online Access:https://www.mdpi.com/2073-4344/12/6/575
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author Felipe de J. Silerio-Vázquez
Cynthia M. Núñez-Núñez
María T. Alarcón-Herrera
José B. Proal-Nájera
author_facet Felipe de J. Silerio-Vázquez
Cynthia M. Núñez-Núñez
María T. Alarcón-Herrera
José B. Proal-Nájera
author_sort Felipe de J. Silerio-Vázquez
collection DOAJ
description Phenol is a recalcitrant anthropogenic compound whose presence has been reported in both wastewater and drinking water; human exposure to phenolic substances can lead to health problems. The degradation of phenol (measured as COD decrease) through solar heterogeneous photocatalysis with immobilized TiO<sub>2</sub> was performed in two different reactors: a flat-plate reactor (FPR) and a compound parabolic collector (CPC). A 2<sup>3</sup> full factorial experimental design was followed. The variables were the presence of TiO<sub>2</sub>, H<sub>2</sub>O<sub>2</sub> addition, and the type of reactor. Data were fitted to the pseudo-first-order reaction-rate-kinetics model. The rate constant for photocatalytic phenol degradation with 1 mM of H<sub>2</sub>O<sub>2</sub> was 6.6 × 10<sup>−3</sup> min<sup>−1</sup> for the FPR and 5.9 × 10<sup>−3</sup> min<sup>−1</sup> in the CPC. The calculated figures of merit were analyzed with a MANCOVA, with UV fluence as a covariate. An ANCOVA showed that the type of reactor, H<sub>2</sub>O<sub>2</sub> addition, or fluence had no statistically significant effect on the results, but there was for the presence of TiO<sub>2</sub>. According to the MANCOVA, fluence and TiO<sub>2</sub> presence were significant (<i>p</i> < 0.05). The CPC was on average 17.4% more efficient than the FPR when it came to collector area per order (<i>A<sub>CO</sub></i>) by heterogeneous photocatalysis and 1 mM H<sub>2</sub>O<sub>2</sub> addition.
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spelling doaj.art-ef15870cf4a04dd198724d10caf33ead2023-11-23T15:58:41ZengMDPI AGCatalysts2073-43442022-05-0112657510.3390/catal12060575Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic CollectorFelipe de J. Silerio-Vázquez0Cynthia M. Núñez-Núñez1María T. Alarcón-Herrera2José B. Proal-Nájera3Centro de Investigación en Materiales Avanzados, Departamento de Ingeniería Sustentable, S.C. Calle CIMAV 110, Colonia 15 de Mayo, Durango 34147, MexicoIngeniería en Tecnología Ambiental, Universidad Politécnica de Durango, Carretera Durango-México km 9.5, Durango 34300, MexicoCentro de Investigación en Materiales Avanzados, Departamento de Ingeniería Sustentable, S.C. Calle CIMAV 110, Colonia 15 de Mayo, Durango 34147, MexicoInstituto Politécnico Nacional, CIIDIR-Durango, Calle Sigma 119, Fraccionamiento 20 de Noviembre II, Durango 34220, MexicoPhenol is a recalcitrant anthropogenic compound whose presence has been reported in both wastewater and drinking water; human exposure to phenolic substances can lead to health problems. The degradation of phenol (measured as COD decrease) through solar heterogeneous photocatalysis with immobilized TiO<sub>2</sub> was performed in two different reactors: a flat-plate reactor (FPR) and a compound parabolic collector (CPC). A 2<sup>3</sup> full factorial experimental design was followed. The variables were the presence of TiO<sub>2</sub>, H<sub>2</sub>O<sub>2</sub> addition, and the type of reactor. Data were fitted to the pseudo-first-order reaction-rate-kinetics model. The rate constant for photocatalytic phenol degradation with 1 mM of H<sub>2</sub>O<sub>2</sub> was 6.6 × 10<sup>−3</sup> min<sup>−1</sup> for the FPR and 5.9 × 10<sup>−3</sup> min<sup>−1</sup> in the CPC. The calculated figures of merit were analyzed with a MANCOVA, with UV fluence as a covariate. An ANCOVA showed that the type of reactor, H<sub>2</sub>O<sub>2</sub> addition, or fluence had no statistically significant effect on the results, but there was for the presence of TiO<sub>2</sub>. According to the MANCOVA, fluence and TiO<sub>2</sub> presence were significant (<i>p</i> < 0.05). The CPC was on average 17.4% more efficient than the FPR when it came to collector area per order (<i>A<sub>CO</sub></i>) by heterogeneous photocatalysis and 1 mM H<sub>2</sub>O<sub>2</sub> addition.https://www.mdpi.com/2073-4344/12/6/575solar irradiancetitanium dioxidebatch modefigures of meritfluencecollector area per order
spellingShingle Felipe de J. Silerio-Vázquez
Cynthia M. Núñez-Núñez
María T. Alarcón-Herrera
José B. Proal-Nájera
Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
Catalysts
solar irradiance
titanium dioxide
batch mode
figures of merit
fluence
collector area per order
title Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
title_full Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
title_fullStr Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
title_full_unstemmed Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
title_short Comparative Efficiencies for Phenol Degradation on Solar Heterogeneous Photocatalytic Reactors: Flat Plate and Compound Parabolic Collector
title_sort comparative efficiencies for phenol degradation on solar heterogeneous photocatalytic reactors flat plate and compound parabolic collector
topic solar irradiance
titanium dioxide
batch mode
figures of merit
fluence
collector area per order
url https://www.mdpi.com/2073-4344/12/6/575
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