Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite

Arsenate As(V) is a toxic contaminant commonly found in aquifers and groundwater that poses significant risks to human health. The effective treatment of arseniccontaminated water is therefore crucial for safeguarding public health. This study investigates removing As(V) using iron oxide-coated igni...

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Autores principales: Velarde Apaza, Lelie Diana, Chávez Collantes, Azucena, Solórzano Acosta, Richard Andi, Cuevas Gimenez, Juan Pablo, Villanueva Salas, José Antonio
Formato: Artículo
Lenguaje:Inglés
Publicado: MDPI 2025
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Acceso en línea:http://hdl.handle.net/20.500.12955/2702
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author Velarde Apaza, Lelie Diana
Chávez Collantes, Azucena
Solórzano Acosta, Richard Andi
Cuevas Gimenez, Juan Pablo
Villanueva Salas, José Antonio
author_browse Chávez Collantes, Azucena
Cuevas Gimenez, Juan Pablo
Solórzano Acosta, Richard Andi
Velarde Apaza, Lelie Diana
Villanueva Salas, José Antonio
author_facet Velarde Apaza, Lelie Diana
Chávez Collantes, Azucena
Solórzano Acosta, Richard Andi
Cuevas Gimenez, Juan Pablo
Villanueva Salas, José Antonio
author_sort Velarde Apaza, Lelie Diana
collection Repositorio INIA
description Arsenate As(V) is a toxic contaminant commonly found in aquifers and groundwater that poses significant risks to human health. The effective treatment of arseniccontaminated water is therefore crucial for safeguarding public health. This study investigates removing As(V) using iron oxide-coated ignimbrite in batch experiments by varying the adsorbent dosage, initial As(V) concentration, contact time, and system temperature. The adsorption experiments revealed that the Langmuir isotherm model better fit the data (R2 = 0.99) than the Freundlich model (R2 = 0.73). According to the Langmuir model, the maximum adsorption capacity of As(V) on the iron oxide-coated ignimbrite was 4.84 mg·g −1 ± 0.12 mg·g −1 of As(V), with a standard deviation of ±0.05 mg·g −1 after 2 h of exposure with 0.15 g/50 mL iron oxide-coated ignimbrite adsorbent concentration. In the kinetic analysis, the pseudo-first-order model best described the adsorption process at 283 K, 293 K, and 303 K, although the pseudo-second-order model also showed an adequate fit, particularly at 293 K. This indicates that, while the pseudo-first-order model is generally more suitable under these conditions, the pseudo-second-order model may also apply under certain circumstances. The results of the batch experiments demonstrate that iron oxide-coated ignimbrite is a promising adsorbent for effectively reducing high concentrations of As(V) in contaminated water
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spelling INIA27022025-09-18T20:29:50Z Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite Velarde Apaza, Lelie Diana Chávez Collantes, Azucena Solórzano Acosta, Richard Andi Cuevas Gimenez, Juan Pablo Villanueva Salas, José Antonio Arsenic(V) ignimbrite iron oxide metal removal adsorption underground water. https://purl.org/pe-repo/ocde/ford#4.01.01 https://purl.org/pe-repo/ocde/ford#4.05.00 Arsenic Arsenate As(V) is a toxic contaminant commonly found in aquifers and groundwater that poses significant risks to human health. The effective treatment of arseniccontaminated water is therefore crucial for safeguarding public health. This study investigates removing As(V) using iron oxide-coated ignimbrite in batch experiments by varying the adsorbent dosage, initial As(V) concentration, contact time, and system temperature. The adsorption experiments revealed that the Langmuir isotherm model better fit the data (R2 = 0.99) than the Freundlich model (R2 = 0.73). According to the Langmuir model, the maximum adsorption capacity of As(V) on the iron oxide-coated ignimbrite was 4.84 mg·g −1 ± 0.12 mg·g −1 of As(V), with a standard deviation of ±0.05 mg·g −1 after 2 h of exposure with 0.15 g/50 mL iron oxide-coated ignimbrite adsorbent concentration. In the kinetic analysis, the pseudo-first-order model best described the adsorption process at 283 K, 293 K, and 303 K, although the pseudo-second-order model also showed an adequate fit, particularly at 293 K. This indicates that, while the pseudo-first-order model is generally more suitable under these conditions, the pseudo-second-order model may also apply under certain circumstances. The results of the batch experiments demonstrate that iron oxide-coated ignimbrite is a promising adsorbent for effectively reducing high concentrations of As(V) in contaminated water 2025-04-01T20:37:38Z 2025-04-01T20:37:38Z 2024-12-28 info:eu-repo/semantics/article Velarde-Apaza, L.D., Chávez-Collantes, A., Solorzano-Acosta, R., Cuevas, J.-P., Villanueva-Salas, J.A. Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite. Water 2025, 17, 53. DOI: 10.3390/w17010053. http://hdl.handle.net/20.500.12955/2702 10.3390/w17010053 eng 2073-4441 Water 2025 info:eu-repo/semantics/openAccess https://creativecommons.org/licenses/by/4.0/ application/pdf application/pdf MDPI IQ Instituto Nacional de Innovación Agraria Repositorio Institucional - INIA
spellingShingle Arsenic(V)
ignimbrite
iron oxide
metal removal
adsorption
underground water.
https://purl.org/pe-repo/ocde/ford#4.01.01
https://purl.org/pe-repo/ocde/ford#4.05.00
Arsenic
Velarde Apaza, Lelie Diana
Chávez Collantes, Azucena
Solórzano Acosta, Richard Andi
Cuevas Gimenez, Juan Pablo
Villanueva Salas, José Antonio
Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title_full Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title_fullStr Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title_full_unstemmed Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title_short Aqueous-Medium Arsenic(V) Removal Using Iron Oxide-Coated Ignimbrite
title_sort aqueous medium arsenic v removal using iron oxide coated ignimbrite
topic Arsenic(V)
ignimbrite
iron oxide
metal removal
adsorption
underground water.
https://purl.org/pe-repo/ocde/ford#4.01.01
https://purl.org/pe-repo/ocde/ford#4.05.00
Arsenic
url http://hdl.handle.net/20.500.12955/2702
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