Hexavalent chromium removal by ferrochromium slag

The aim of this study is to demonstrate the potential of Cr(VI) generation during jigging operation applied for ferrochrome recovery from slag. The Cr(VI) concentration s of water contacted with ferrochromium slag (W/FS = 10) in a closed cycle after 50 batches were found as 0.61 mg/l. Also, reductio...

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Veröffentlicht in:Journal of hazardous materials 2005-11, Vol.126 (1), p.176-182
Hauptverfasser: Erdem, Mehmet, Altundoğan, H. Soner, Turan, M. Deniz, Tümen, Fikret
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container_issue 1
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container_title Journal of hazardous materials
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creator Erdem, Mehmet
Altundoğan, H. Soner
Turan, M. Deniz
Tümen, Fikret
description The aim of this study is to demonstrate the potential of Cr(VI) generation during jigging operation applied for ferrochrome recovery from slag. The Cr(VI) concentration s of water contacted with ferrochromium slag (W/FS = 10) in a closed cycle after 50 batches were found as 0.61 mg/l. Also, reduction of Cr(VI) to Cr(III) and a subsequent precipitation of Cr(III) by using ferrochrome slag (FS) in a model solution has been aimed. The effects of amount of acid, contact time, FS dosage, initial Cr(VI) concentration and temperature on the Cr(VI) reduction have been studied through the batch runs. The amount of acid has been found to be the most effective parameter affecting the Cr(VI) reduction. A 10 g/l FS dosage and 3.5 ml/l H 2SO 4 (5 M) are sufficient to reduce all Cr(VI) in the model solution containing 10 mg/l Cr(VI) and for contact time of 60 min at 25 °C. In reduced solutions, precipitation of metal ions has been studied by using extra FS. A 60 g/l dosage of fresh FS can precipitate all Cr(III) and Fe ions in the reduced solution. Thus, it has been demonstrated that the treatment of jigging water stream to be generated in a ferrochrome plant containing Cr(VI) can be accomplished by using ferrochromium slag and sulphuric acid. Also, it has been determined that solid residues of the process are environmentally stable by applying TCLP test.
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A 10 g/l FS dosage and 3.5 ml/l H 2SO 4 (5 M) are sufficient to reduce all Cr(VI) in the model solution containing 10 mg/l Cr(VI) and for contact time of 60 min at 25 °C. In reduced solutions, precipitation of metal ions has been studied by using extra FS. A 60 g/l dosage of fresh FS can precipitate all Cr(III) and Fe ions in the reduced solution. Thus, it has been demonstrated that the treatment of jigging water stream to be generated in a ferrochrome plant containing Cr(VI) can be accomplished by using ferrochromium slag and sulphuric acid. 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Soner</creatorcontrib><creatorcontrib>Turan, M. Deniz</creatorcontrib><creatorcontrib>Tümen, Fikret</creatorcontrib><title>Hexavalent chromium removal by ferrochromium slag</title><title>Journal of hazardous materials</title><addtitle>J Hazard Mater</addtitle><description>The aim of this study is to demonstrate the potential of Cr(VI) generation during jigging operation applied for ferrochrome recovery from slag. The Cr(VI) concentration s of water contacted with ferrochromium slag (W/FS = 10) in a closed cycle after 50 batches were found as 0.61 mg/l. Also, reduction of Cr(VI) to Cr(III) and a subsequent precipitation of Cr(III) by using ferrochrome slag (FS) in a model solution has been aimed. The effects of amount of acid, contact time, FS dosage, initial Cr(VI) concentration and temperature on the Cr(VI) reduction have been studied through the batch runs. The amount of acid has been found to be the most effective parameter affecting the Cr(VI) reduction. A 10 g/l FS dosage and 3.5 ml/l H 2SO 4 (5 M) are sufficient to reduce all Cr(VI) in the model solution containing 10 mg/l Cr(VI) and for contact time of 60 min at 25 °C. In reduced solutions, precipitation of metal ions has been studied by using extra FS. A 60 g/l dosage of fresh FS can precipitate all Cr(III) and Fe ions in the reduced solution. Thus, it has been demonstrated that the treatment of jigging water stream to be generated in a ferrochrome plant containing Cr(VI) can be accomplished by using ferrochromium slag and sulphuric acid. Also, it has been determined that solid residues of the process are environmentally stable by applying TCLP test.</description><subject>Applied sciences</subject><subject>Calcium Carbonate</subject><subject>Carbonates</subject><subject>Chromium - isolation &amp; purification</subject><subject>Chromium Alloys - chemistry</subject><subject>Citrates</subject><subject>Continental surface waters</subject><subject>Drug Combinations</subject><subject>Exact sciences and technology</subject><subject>Ferrochromium slag</subject><subject>Heavy metal removal</subject><subject>Hexavalent chromium</subject><subject>Hydrogen-Ion Concentration</subject><subject>Industrial Waste - prevention &amp; control</subject><subject>Magnesium Oxide</subject><subject>Natural water pollution</subject><subject>Osmolar Concentration</subject><subject>Other industrial wastes. 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subjects Applied sciences
Calcium Carbonate
Carbonates
Chromium - isolation & purification
Chromium Alloys - chemistry
Citrates
Continental surface waters
Drug Combinations
Exact sciences and technology
Ferrochromium slag
Heavy metal removal
Hexavalent chromium
Hydrogen-Ion Concentration
Industrial Waste - prevention & control
Magnesium Oxide
Natural water pollution
Osmolar Concentration
Other industrial wastes. Sewage sludge
Pollution
Reduction
TCLP
Temperature
Wastes
Water
Water treatment and pollution
title Hexavalent chromium removal by ferrochromium slag
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