Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD
The use of electrochemistry is a promising approach for the treatment of direct osmosis concentrate that contains a high concentration of organic pollutants and has high osmotic pressure, to achieve the safe discharge of effluent. This work addresses, for the first time, this major environmental cha...
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MDPI AG
2021
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oai:doaj.org-article:a31880a584bf41c48a89631824ebb9262021-11-11T19:58:25ZElectrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD10.3390/w132131362073-4441https://doaj.org/article/a31880a584bf41c48a89631824ebb9262021-11-01T00:00:00Zhttps://www.mdpi.com/2073-4441/13/21/3136https://doaj.org/toc/2073-4441The use of electrochemistry is a promising approach for the treatment of direct osmosis concentrate that contains a high concentration of organic pollutants and has high osmotic pressure, to achieve the safe discharge of effluent. This work addresses, for the first time, this major environmental challenge using perforated aluminum electrodes mounted in an electrocoagulation–flotation cell (PA-ECF). The design of the experiments, the modeling, and the optimization of the PA-ECF conditions for the treatment of DO concentrate rich in Pb were explored using a central composite design (CCD) under response surface methodology (RSM). Therefore, the CCD-RSM was employed to optimize and study the effect of the independent variables, namely electrolysis time (5.85 min to 116.15 min) and current intensity (0.09 A to 2.91 A) on Pb removal. Optimal values of the process parameters were determined as an electrolysis time of 77.65 min and a current intensity of 0.9 A. In addition to Pb removal (97.8%), energy consumption, electrode mass-consumed material, and operating cost were estimated as 0.0025 kWh/m<sup>3</sup>, 0.217 kg Al/m<sup>3</sup>, and 0.423 USD/m<sup>3</sup>, respectively. In addition, it was found that DO concentrate obtained from metallurgical wastewater can be recovered through PA-ECF (almost 94% Pb removal). This work demonstrated that the PA-ECF technique could became a viable process applicable in the treatment of DO concentrate containing Pb-rich for reuse.Milaad MoosazadeRazieh AshooriHamid MoghimiMohammad Ali AmaniZacharias FrontistisRamezan Ali TaheriMDPI AGarticleelectrocoagulation–flotation processperforated aluminumfeed solutiondirect osmosisresponse surface methodologyHydraulic engineeringTC1-978Water supply for domestic and industrial purposesTD201-500ENWater, Vol 13, Iss 3136, p 3136 (2021) |
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electrocoagulation–flotation process perforated aluminum feed solution direct osmosis response surface methodology Hydraulic engineering TC1-978 Water supply for domestic and industrial purposes TD201-500 |
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electrocoagulation–flotation process perforated aluminum feed solution direct osmosis response surface methodology Hydraulic engineering TC1-978 Water supply for domestic and industrial purposes TD201-500 Milaad Moosazade Razieh Ashoori Hamid Moghimi Mohammad Ali Amani Zacharias Frontistis Ramezan Ali Taheri Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
description |
The use of electrochemistry is a promising approach for the treatment of direct osmosis concentrate that contains a high concentration of organic pollutants and has high osmotic pressure, to achieve the safe discharge of effluent. This work addresses, for the first time, this major environmental challenge using perforated aluminum electrodes mounted in an electrocoagulation–flotation cell (PA-ECF). The design of the experiments, the modeling, and the optimization of the PA-ECF conditions for the treatment of DO concentrate rich in Pb were explored using a central composite design (CCD) under response surface methodology (RSM). Therefore, the CCD-RSM was employed to optimize and study the effect of the independent variables, namely electrolysis time (5.85 min to 116.15 min) and current intensity (0.09 A to 2.91 A) on Pb removal. Optimal values of the process parameters were determined as an electrolysis time of 77.65 min and a current intensity of 0.9 A. In addition to Pb removal (97.8%), energy consumption, electrode mass-consumed material, and operating cost were estimated as 0.0025 kWh/m<sup>3</sup>, 0.217 kg Al/m<sup>3</sup>, and 0.423 USD/m<sup>3</sup>, respectively. In addition, it was found that DO concentrate obtained from metallurgical wastewater can be recovered through PA-ECF (almost 94% Pb removal). This work demonstrated that the PA-ECF technique could became a viable process applicable in the treatment of DO concentrate containing Pb-rich for reuse. |
format |
article |
author |
Milaad Moosazade Razieh Ashoori Hamid Moghimi Mohammad Ali Amani Zacharias Frontistis Ramezan Ali Taheri |
author_facet |
Milaad Moosazade Razieh Ashoori Hamid Moghimi Mohammad Ali Amani Zacharias Frontistis Ramezan Ali Taheri |
author_sort |
Milaad Moosazade |
title |
Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
title_short |
Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
title_full |
Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
title_fullStr |
Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
title_full_unstemmed |
Electrochemical Recovery to Overcome Direct Osmosis Concentrate-Bearing Lead: Optimization of Treatment Process via RSM-CCD |
title_sort |
electrochemical recovery to overcome direct osmosis concentrate-bearing lead: optimization of treatment process via rsm-ccd |
publisher |
MDPI AG |
publishDate |
2021 |
url |
https://doaj.org/article/a31880a584bf41c48a89631824ebb926 |
work_keys_str_mv |
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