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Preparation and photocatalytic performance of reduced graphene oxide/ ZnO nanocatalyst for degradation of metalaxyl from aqueous solution: effect of operational parameters, mineralisation and toxicity bioassay

A heterogeneous photocatalyst, ZnO/reduced graphene oxide (ZnO/rGO or ZG), was synthesised for the photocatalytic degradation of metalaxyl (MX) in aqueous solutions under UV irradiation. The characteristics of the prepared catalyst were determined by FTIR, XRD, FE-SEM, EDS, and BET analyses. The eff...

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Published in:International journal of environmental analytical chemistry 2022-12, Vol.102 (18), p.7112-7134
Main Authors: Dehghan, Samaneh, Tahergorabi, Mahsa, Norzaee, Samira, Boorboor Azimi, Elham, Hasham Firooz, Masoumeh, Dadban Shahamat, Yousef
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container_title International journal of environmental analytical chemistry
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Tahergorabi, Mahsa
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Dadban Shahamat, Yousef
description A heterogeneous photocatalyst, ZnO/reduced graphene oxide (ZnO/rGO or ZG), was synthesised for the photocatalytic degradation of metalaxyl (MX) in aqueous solutions under UV irradiation. The characteristics of the prepared catalyst were determined by FTIR, XRD, FE-SEM, EDS, and BET analyses. The effect of various parameters such as solution pH, catalyst concentration, rGO loading in the catalyst structure, MX concentration and UV light intensity on the photodegradation of MX was investigated. The concentration of MX and the toxicity of the intermediates were determined by HPLC and the Daphnia Magna toxicity test, respectively. The effect of the water anions and radical scavenger compounds on the MX removal process was studied as well. The rate of mineralisation was determined by measuring the total organic carbon (TOC) value using the TOC analyser. The efficiency of the degradation process was compared with the real sample of agricultural drainage and deionised water. At optimum conditions (pH = 7, catalyst loading = 10%, catalyst concentration = 0.75 g/l, MX concentration = 10 mg/l, and UV intensity = 220 MW/cm 2 ), the removal and mineralisation rates were 90.25% and 51.17% after 120 min, respectively. Reactive species scavenging experiments showed that the hole was the most effective factor for MX degradation in the ZG/UV process. The MX degradation rate in real agricultural run-off samples showed that the degradation efficiency was 50.42%, which was significantly lower than that of the synthetic samples. The toxicity bioassay by D. Magna indicated that the toxicity of MX was reduced from 51.22 to 15.17 after 96 h during the ZnO/rGO process. The photocatalytic efficiency decreased in the presence of phosphate and nitrate ions but did not change much in the presence of other water anions. Thus, the ZG/UV process can be effectively used for the degradation of organic pollutants, especially pesticides in wastewater.
doi_str_mv 10.1080/03067319.2020.1826461
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The characteristics of the prepared catalyst were determined by FTIR, XRD, FE-SEM, EDS, and BET analyses. The effect of various parameters such as solution pH, catalyst concentration, rGO loading in the catalyst structure, MX concentration and UV light intensity on the photodegradation of MX was investigated. The concentration of MX and the toxicity of the intermediates were determined by HPLC and the Daphnia Magna toxicity test, respectively. The effect of the water anions and radical scavenger compounds on the MX removal process was studied as well. The rate of mineralisation was determined by measuring the total organic carbon (TOC) value using the TOC analyser. The efficiency of the degradation process was compared with the real sample of agricultural drainage and deionised water. At optimum conditions (pH = 7, catalyst loading = 10%, catalyst concentration = 0.75 g/l, MX concentration = 10 mg/l, and UV intensity = 220 MW/cm 2 ), the removal and mineralisation rates were 90.25% and 51.17% after 120 min, respectively. Reactive species scavenging experiments showed that the hole was the most effective factor for MX degradation in the ZG/UV process. The MX degradation rate in real agricultural run-off samples showed that the degradation efficiency was 50.42%, which was significantly lower than that of the synthetic samples. The toxicity bioassay by D. Magna indicated that the toxicity of MX was reduced from 51.22 to 15.17 after 96 h during the ZnO/rGO process. The photocatalytic efficiency decreased in the presence of phosphate and nitrate ions but did not change much in the presence of other water anions. 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At optimum conditions (pH = 7, catalyst loading = 10%, catalyst concentration = 0.75 g/l, MX concentration = 10 mg/l, and UV intensity = 220 MW/cm 2 ), the removal and mineralisation rates were 90.25% and 51.17% after 120 min, respectively. Reactive species scavenging experiments showed that the hole was the most effective factor for MX degradation in the ZG/UV process. The MX degradation rate in real agricultural run-off samples showed that the degradation efficiency was 50.42%, which was significantly lower than that of the synthetic samples. The toxicity bioassay by D. Magna indicated that the toxicity of MX was reduced from 51.22 to 15.17 after 96 h during the ZnO/rGO process. The photocatalytic efficiency decreased in the presence of phosphate and nitrate ions but did not change much in the presence of other water anions. 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The characteristics of the prepared catalyst were determined by FTIR, XRD, FE-SEM, EDS, and BET analyses. The effect of various parameters such as solution pH, catalyst concentration, rGO loading in the catalyst structure, MX concentration and UV light intensity on the photodegradation of MX was investigated. The concentration of MX and the toxicity of the intermediates were determined by HPLC and the Daphnia Magna toxicity test, respectively. The effect of the water anions and radical scavenger compounds on the MX removal process was studied as well. The rate of mineralisation was determined by measuring the total organic carbon (TOC) value using the TOC analyser. The efficiency of the degradation process was compared with the real sample of agricultural drainage and deionised water. At optimum conditions (pH = 7, catalyst loading = 10%, catalyst concentration = 0.75 g/l, MX concentration = 10 mg/l, and UV intensity = 220 MW/cm 2 ), the removal and mineralisation rates were 90.25% and 51.17% after 120 min, respectively. Reactive species scavenging experiments showed that the hole was the most effective factor for MX degradation in the ZG/UV process. The MX degradation rate in real agricultural run-off samples showed that the degradation efficiency was 50.42%, which was significantly lower than that of the synthetic samples. The toxicity bioassay by D. Magna indicated that the toxicity of MX was reduced from 51.22 to 15.17 after 96 h during the ZnO/rGO process. The photocatalytic efficiency decreased in the presence of phosphate and nitrate ions but did not change much in the presence of other water anions. Thus, the ZG/UV process can be effectively used for the degradation of organic pollutants, especially pesticides in wastewater.</abstract><cop>Abingdon</cop><pub>Taylor &amp; Francis</pub><doi>10.1080/03067319.2020.1826461</doi><tpages>23</tpages></addata></record>
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subjects Agricultural runoff
Anions
Aqueous solutions
Bio-assays
Bioassays
Catalysts
Degradation
Efficiency
Freshwater crustaceans
Fungicides
Graphene
HPLC
Intermediates
Irradiation
Light intensity
Liquid chromatography
Luminous intensity
Metalaxyl
Mineralization
Organic carbon
Parameters
Pesticides
pH effects
Phosphates
Photocatalysis
Photodegradation
Pollutants
Removal
Scavenging
Total organic carbon
Toxicity
Toxicity testing
Ultraviolet radiation
Wastewater
Zinc oxide
Zno/reduced graphene oxide
title Preparation and photocatalytic performance of reduced graphene oxide/ ZnO nanocatalyst for degradation of metalaxyl from aqueous solution: effect of operational parameters, mineralisation and toxicity bioassay
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