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The Effectiveness of Zn Leaching from EAFD Using Caustic Soda

Electric arc furnace dust (EAFD) is a toxic waste which is mainly rich in iron oxide, zinc, and lead. Hydrometallurgical extraction of zinc from Jordanian EAFD in alkaline medium was investigated; NaOH, NaHCO 3 , and Na 2 CO 3 were used as leaching agents. The pH values for the prepared solutions we...

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Published in:Water, air, and soil pollution air, and soil pollution, 2018-02, Vol.229 (2), p.1-10, Article 33
Main Authors: Al-Makhadmeh, Leema A., Batiha, Mohammad A., Al-Harahsheh, Mohammad S., Altarawneh, Ibrahem S., Rawadieh, Saleh E.
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Rawadieh, Saleh E.
description Electric arc furnace dust (EAFD) is a toxic waste which is mainly rich in iron oxide, zinc, and lead. Hydrometallurgical extraction of zinc from Jordanian EAFD in alkaline medium was investigated; NaOH, NaHCO 3 , and Na 2 CO 3 were used as leaching agents. The pH values for the prepared solutions were 8.3, 8.2, and 12.55 for NaHCO 3 , Na 2 CO 3 , and NaOH, respectively. The effect of NaOH concentration (1, 3, 5, 7, and 9 M), contact time (5 min to 3 h), temperature (20, 40, and 60), and solid-to-liquid ratio (SLR; 20, 40, 80, and 120 mg/ml) on the leachability of zinc from EAFD were tested. The initial EAFD and the resulting leach residues were characterized using X-ray diffraction (XRD) and X-ray fluorescence (XRF). EAFD contained 25.9% Zn, 18.0% Fe, and 3.2% Pb. A maximum zinc recovery of 92.9% was achieved using 6 M NaOH at 60 °C with solid loading of 20 g/L and 3 h leaching time. NaHCO 3 and Na 2 CO 3 were not efficient leaching agents for Zn extraction since the recoveries were only 2.6 and 4.5%, respectively. Zn and Pb were depleted in the residues with an E -factor of 0.5–0.6 and 0.1–0.25, respectively. Iron was enriched in the residues; the E -factor was around 2. The EAFD contained mainly zincite, franklinite, and magnetite. After 3 h leaching, only traces of zincite exist in the residues, while sylvite and halite were completely dissolved.
doi_str_mv 10.1007/s11270-018-3694-4
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Hydrometallurgical extraction of zinc from Jordanian EAFD in alkaline medium was investigated; NaOH, NaHCO 3 , and Na 2 CO 3 were used as leaching agents. The pH values for the prepared solutions were 8.3, 8.2, and 12.55 for NaHCO 3 , Na 2 CO 3 , and NaOH, respectively. The effect of NaOH concentration (1, 3, 5, 7, and 9 M), contact time (5 min to 3 h), temperature (20, 40, and 60), and solid-to-liquid ratio (SLR; 20, 40, 80, and 120 mg/ml) on the leachability of zinc from EAFD were tested. The initial EAFD and the resulting leach residues were characterized using X-ray diffraction (XRD) and X-ray fluorescence (XRF). EAFD contained 25.9% Zn, 18.0% Fe, and 3.2% Pb. A maximum zinc recovery of 92.9% was achieved using 6 M NaOH at 60 °C with solid loading of 20 g/L and 3 h leaching time. NaHCO 3 and Na 2 CO 3 were not efficient leaching agents for Zn extraction since the recoveries were only 2.6 and 4.5%, respectively. Zn and Pb were depleted in the residues with an E -factor of 0.5–0.6 and 0.1–0.25, respectively. Iron was enriched in the residues; the E -factor was around 2. The EAFD contained mainly zincite, franklinite, and magnetite. After 3 h leaching, only traces of zincite exist in the residues, while sylvite and halite were completely dissolved.</description><identifier>ISSN: 0049-6979</identifier><identifier>EISSN: 1573-2932</identifier><identifier>DOI: 10.1007/s11270-018-3694-4</identifier><language>eng</language><publisher>Cham: Springer International Publishing</publisher><subject>Atmospheric particulates ; Atmospheric Protection/Air Quality Control/Air Pollution ; Caustic leaching ; Caustic soda ; Chemical engineering ; Climate Change/Climate Change Impacts ; Dust ; Dust storms ; Earth and Environmental Science ; Electric contacts ; Environment ; Environmental monitoring ; Ferric oxide ; Fluorescence ; Furnaces ; Halite ; Halites ; Hazardous wastes ; Hydrogeology ; Hydrometallurgy ; Iron ; Iron compounds ; Iron oxides ; Leaching ; Lead ; Magnetite ; Metals ; pH effects ; Recycling ; Residues ; Sodium hydroxide ; Soil Science &amp; Conservation ; Solutions ; Sylvite ; Toxic wastes ; Water Quality/Water Pollution ; X-ray diffraction ; X-ray fluorescence ; X-ray spectroscopy ; X-rays ; Zinc ; Zinc oxide ; Zinc oxides</subject><ispartof>Water, air, and soil pollution, 2018-02, Vol.229 (2), p.1-10, Article 33</ispartof><rights>Springer International Publishing AG, part of Springer Nature 2018</rights><rights>COPYRIGHT 2018 Springer</rights><rights>Water, Air, &amp; Soil Pollution is a copyright of Springer, (2018). 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Hydrometallurgical extraction of zinc from Jordanian EAFD in alkaline medium was investigated; NaOH, NaHCO 3 , and Na 2 CO 3 were used as leaching agents. The pH values for the prepared solutions were 8.3, 8.2, and 12.55 for NaHCO 3 , Na 2 CO 3 , and NaOH, respectively. The effect of NaOH concentration (1, 3, 5, 7, and 9 M), contact time (5 min to 3 h), temperature (20, 40, and 60), and solid-to-liquid ratio (SLR; 20, 40, 80, and 120 mg/ml) on the leachability of zinc from EAFD were tested. The initial EAFD and the resulting leach residues were characterized using X-ray diffraction (XRD) and X-ray fluorescence (XRF). EAFD contained 25.9% Zn, 18.0% Fe, and 3.2% Pb. A maximum zinc recovery of 92.9% was achieved using 6 M NaOH at 60 °C with solid loading of 20 g/L and 3 h leaching time. NaHCO 3 and Na 2 CO 3 were not efficient leaching agents for Zn extraction since the recoveries were only 2.6 and 4.5%, respectively. Zn and Pb were depleted in the residues with an E -factor of 0.5–0.6 and 0.1–0.25, respectively. Iron was enriched in the residues; the E -factor was around 2. The EAFD contained mainly zincite, franklinite, and magnetite. After 3 h leaching, only traces of zincite exist in the residues, while sylvite and halite were completely dissolved.</description><subject>Atmospheric particulates</subject><subject>Atmospheric Protection/Air Quality Control/Air Pollution</subject><subject>Caustic leaching</subject><subject>Caustic soda</subject><subject>Chemical engineering</subject><subject>Climate Change/Climate Change Impacts</subject><subject>Dust</subject><subject>Dust storms</subject><subject>Earth and Environmental Science</subject><subject>Electric contacts</subject><subject>Environment</subject><subject>Environmental monitoring</subject><subject>Ferric oxide</subject><subject>Fluorescence</subject><subject>Furnaces</subject><subject>Halite</subject><subject>Halites</subject><subject>Hazardous wastes</subject><subject>Hydrogeology</subject><subject>Hydrometallurgy</subject><subject>Iron</subject><subject>Iron compounds</subject><subject>Iron oxides</subject><subject>Leaching</subject><subject>Lead</subject><subject>Magnetite</subject><subject>Metals</subject><subject>pH effects</subject><subject>Recycling</subject><subject>Residues</subject><subject>Sodium hydroxide</subject><subject>Soil Science &amp; 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Hydrometallurgical extraction of zinc from Jordanian EAFD in alkaline medium was investigated; NaOH, NaHCO 3 , and Na 2 CO 3 were used as leaching agents. The pH values for the prepared solutions were 8.3, 8.2, and 12.55 for NaHCO 3 , Na 2 CO 3 , and NaOH, respectively. The effect of NaOH concentration (1, 3, 5, 7, and 9 M), contact time (5 min to 3 h), temperature (20, 40, and 60), and solid-to-liquid ratio (SLR; 20, 40, 80, and 120 mg/ml) on the leachability of zinc from EAFD were tested. The initial EAFD and the resulting leach residues were characterized using X-ray diffraction (XRD) and X-ray fluorescence (XRF). EAFD contained 25.9% Zn, 18.0% Fe, and 3.2% Pb. A maximum zinc recovery of 92.9% was achieved using 6 M NaOH at 60 °C with solid loading of 20 g/L and 3 h leaching time. NaHCO 3 and Na 2 CO 3 were not efficient leaching agents for Zn extraction since the recoveries were only 2.6 and 4.5%, respectively. Zn and Pb were depleted in the residues with an E -factor of 0.5–0.6 and 0.1–0.25, respectively. Iron was enriched in the residues; the E -factor was around 2. The EAFD contained mainly zincite, franklinite, and magnetite. After 3 h leaching, only traces of zincite exist in the residues, while sylvite and halite were completely dissolved.</abstract><cop>Cham</cop><pub>Springer International Publishing</pub><doi>10.1007/s11270-018-3694-4</doi><tpages>10</tpages></addata></record>
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subjects Atmospheric particulates
Atmospheric Protection/Air Quality Control/Air Pollution
Caustic leaching
Caustic soda
Chemical engineering
Climate Change/Climate Change Impacts
Dust
Dust storms
Earth and Environmental Science
Electric contacts
Environment
Environmental monitoring
Ferric oxide
Fluorescence
Furnaces
Halite
Halites
Hazardous wastes
Hydrogeology
Hydrometallurgy
Iron
Iron compounds
Iron oxides
Leaching
Lead
Magnetite
Metals
pH effects
Recycling
Residues
Sodium hydroxide
Soil Science & Conservation
Solutions
Sylvite
Toxic wastes
Water Quality/Water Pollution
X-ray diffraction
X-ray fluorescence
X-ray spectroscopy
X-rays
Zinc
Zinc oxide
Zinc oxides
title The Effectiveness of Zn Leaching from EAFD Using Caustic Soda
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