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Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption

Arsenic (As(III)), more toxic and with less affinity than arsenate (As(V)), is hard to remove from the aqueous phase due to the lack of efficient adsorbents. In this study, a core–shell structured MnO(2)@La(OH)(3) nanocomposite was synthesized via a facile two-step precipitation method. Its removal...

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Detalles Bibliográficos
Autores principales: Wang, Yulong, Guo, Chen, Zhang, Lin, Lu, Xihao, Liu, Yanhong, Li, Xuhui, Wang, Yangyang, Wang, Shaofeng
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2022
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9518204/
https://www.ncbi.nlm.nih.gov/pubmed/36078364
http://dx.doi.org/10.3390/ijerph191710649
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author Wang, Yulong
Guo, Chen
Zhang, Lin
Lu, Xihao
Liu, Yanhong
Li, Xuhui
Wang, Yangyang
Wang, Shaofeng
author_facet Wang, Yulong
Guo, Chen
Zhang, Lin
Lu, Xihao
Liu, Yanhong
Li, Xuhui
Wang, Yangyang
Wang, Shaofeng
author_sort Wang, Yulong
collection PubMed
description Arsenic (As(III)), more toxic and with less affinity than arsenate (As(V)), is hard to remove from the aqueous phase due to the lack of efficient adsorbents. In this study, a core–shell structured MnO(2)@La(OH)(3) nanocomposite was synthesized via a facile two-step precipitation method. Its removal performance and mechanisms for As(V) and As(III) were investigated through batch adsorption experiments and a series of analysis methods including the transformation kinetics of arsenic species in As(III) removal, FTIR, XRD and XPS. Solution pH could significantly influence the removal efficiencies of arsenic. The adsorption process of As(V) occurred rapidly in the first 5 h and then gradually decreased, whereas the As(III) removal rate was relatively slower. The maximum adsorption capacities of As(V) and As(III) were up to 138.9 and 139.9 mg/g at pH 4.0, respectively. For As(V) removal, the inner-sphere complexes of lanthanum arsenate were formed through the ligand exchange reactions and coprecipitation. The oxidation of As(III) to the less toxic As(V) by δ-MnO(2) and subsequently the synergistic adsorption process by the lanthanum hydroxide on the MnO(2)@La(OH)(3) nanocomposite to form lanthanum arsenate were the dominant mechanisms of As(III) removal. XPS analysis indicated that approximately 20.6% of Mn in the nanocomposite after As(III) removal were Mn(II). Furthermore, a small amount of Mn(II) and La(III) were released into solution during the process of As(III) removal. These results confirm its efficient performance in the arsenic-containing water treatment, such as As(III)-contaminated groundwater used for irrigation and As(V)-contaminated industrial wastewater.
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spelling pubmed-95182042022-09-29 Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption Wang, Yulong Guo, Chen Zhang, Lin Lu, Xihao Liu, Yanhong Li, Xuhui Wang, Yangyang Wang, Shaofeng Int J Environ Res Public Health Article Arsenic (As(III)), more toxic and with less affinity than arsenate (As(V)), is hard to remove from the aqueous phase due to the lack of efficient adsorbents. In this study, a core–shell structured MnO(2)@La(OH)(3) nanocomposite was synthesized via a facile two-step precipitation method. Its removal performance and mechanisms for As(V) and As(III) were investigated through batch adsorption experiments and a series of analysis methods including the transformation kinetics of arsenic species in As(III) removal, FTIR, XRD and XPS. Solution pH could significantly influence the removal efficiencies of arsenic. The adsorption process of As(V) occurred rapidly in the first 5 h and then gradually decreased, whereas the As(III) removal rate was relatively slower. The maximum adsorption capacities of As(V) and As(III) were up to 138.9 and 139.9 mg/g at pH 4.0, respectively. For As(V) removal, the inner-sphere complexes of lanthanum arsenate were formed through the ligand exchange reactions and coprecipitation. The oxidation of As(III) to the less toxic As(V) by δ-MnO(2) and subsequently the synergistic adsorption process by the lanthanum hydroxide on the MnO(2)@La(OH)(3) nanocomposite to form lanthanum arsenate were the dominant mechanisms of As(III) removal. XPS analysis indicated that approximately 20.6% of Mn in the nanocomposite after As(III) removal were Mn(II). Furthermore, a small amount of Mn(II) and La(III) were released into solution during the process of As(III) removal. These results confirm its efficient performance in the arsenic-containing water treatment, such as As(III)-contaminated groundwater used for irrigation and As(V)-contaminated industrial wastewater. MDPI 2022-08-26 /pmc/articles/PMC9518204/ /pubmed/36078364 http://dx.doi.org/10.3390/ijerph191710649 Text en © 2022 by the authors. https://creativecommons.org/licenses/by/4.0/Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (https://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Wang, Yulong
Guo, Chen
Zhang, Lin
Lu, Xihao
Liu, Yanhong
Li, Xuhui
Wang, Yangyang
Wang, Shaofeng
Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title_full Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title_fullStr Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title_full_unstemmed Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title_short Arsenic Oxidation and Removal from Water via Core–Shell MnO(2)@La(OH)(3) Nanocomposite Adsorption
title_sort arsenic oxidation and removal from water via core–shell mno(2)@la(oh)(3) nanocomposite adsorption
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC9518204/
https://www.ncbi.nlm.nih.gov/pubmed/36078364
http://dx.doi.org/10.3390/ijerph191710649
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