Treatment of iron(II)-rich acid mine water with limestone and oxygen

The main components of acid mine water are free acid, sulphate, and Fe²⁺. Limestone is the most cost-effective alkali that can be used for neutralization. The purpose of this investigation was to identify conditions where Fe²⁺ is removed with limestone and simultaneously oxidized with oxygen to Fe³⁺...

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Veröffentlicht in:Water science and technology 2014-01, Vol.70 (2), p.209-217
Hauptverfasser: MOHAJANE, G. B, MAREE, J. P, PANICHEV, N
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creator MOHAJANE, G. B
MAREE, J. P
PANICHEV, N
description The main components of acid mine water are free acid, sulphate, and Fe²⁺. Limestone is the most cost-effective alkali that can be used for neutralization. The purpose of this investigation was to identify conditions where Fe²⁺ is removed with limestone and simultaneously oxidized with oxygen to Fe³⁺, in a polyvinyl chloride pipe under pressure. Gypsum scaling is prevented by passing rubber balls through the pipe of the so-called Oxygen-Pipe-Neutralization (OPeN) process pilot plant. Two synthetic waters were treated: (A) acid mine water containing 123 mg L⁻¹ Fe²⁺ representing gold mine water, and (B) acid mine water containing 6,032 mg L⁻¹ Fe²⁺ representing coal mine water. Batch studies were carried out in a pipe reactor and showed that the rate of Fe²⁺ oxidation depended on the Fe²⁺ concentration, oxygen pressure, amount of recycled sludge, limestone dosage and the mixing rate. Continuous studies in an OPeN process pilot plant resulted in 100% removal of total acidity from synthetic coal mine water and a 98% removal from synthetic gold mine water. Fe²⁺ was removed completely as precipitated Fe(OH)₃ from both synthetic coal and gold mine water at around pH 7 at 200 and 100 kPa oxygen pressure, respectively.
doi_str_mv 10.2166/wst.2014.178
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B ; MAREE, J. P ; PANICHEV, N</creator><creatorcontrib>MOHAJANE, G. B ; MAREE, J. P ; PANICHEV, N</creatorcontrib><description>The main components of acid mine water are free acid, sulphate, and Fe²⁺. Limestone is the most cost-effective alkali that can be used for neutralization. The purpose of this investigation was to identify conditions where Fe²⁺ is removed with limestone and simultaneously oxidized with oxygen to Fe³⁺, in a polyvinyl chloride pipe under pressure. Gypsum scaling is prevented by passing rubber balls through the pipe of the so-called Oxygen-Pipe-Neutralization (OPeN) process pilot plant. Two synthetic waters were treated: (A) acid mine water containing 123 mg L⁻¹ Fe²⁺ representing gold mine water, and (B) acid mine water containing 6,032 mg L⁻¹ Fe²⁺ representing coal mine water. 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B</au><au>MAREE, J. P</au><au>PANICHEV, N</au><format>journal</format><genre>article</genre><ristype>JOUR</ristype><atitle>Treatment of iron(II)-rich acid mine water with limestone and oxygen</atitle><jtitle>Water science and technology</jtitle><addtitle>Water Sci Technol</addtitle><date>2014-01-01</date><risdate>2014</risdate><volume>70</volume><issue>2</issue><spage>209</spage><epage>217</epage><pages>209-217</pages><issn>0273-1223</issn><eissn>1996-9732</eissn><coden>WSTED4</coden><abstract>The main components of acid mine water are free acid, sulphate, and Fe²⁺. Limestone is the most cost-effective alkali that can be used for neutralization. The purpose of this investigation was to identify conditions where Fe²⁺ is removed with limestone and simultaneously oxidized with oxygen to Fe³⁺, in a polyvinyl chloride pipe under pressure. Gypsum scaling is prevented by passing rubber balls through the pipe of the so-called Oxygen-Pipe-Neutralization (OPeN) process pilot plant. Two synthetic waters were treated: (A) acid mine water containing 123 mg L⁻¹ Fe²⁺ representing gold mine water, and (B) acid mine water containing 6,032 mg L⁻¹ Fe²⁺ representing coal mine water. Batch studies were carried out in a pipe reactor and showed that the rate of Fe²⁺ oxidation depended on the Fe²⁺ concentration, oxygen pressure, amount of recycled sludge, limestone dosage and the mixing rate. Continuous studies in an OPeN process pilot plant resulted in 100% removal of total acidity from synthetic coal mine water and a 98% removal from synthetic gold mine water. Fe²⁺ was removed completely as precipitated Fe(OH)₃ from both synthetic coal and gold mine water at around pH 7 at 200 and 100 kPa oxygen pressure, respectively.</abstract><cop>London</cop><pub>International Water Association</pub><pmid>25051466</pmid><doi>10.2166/wst.2014.178</doi><tpages>9</tpages></addata></record>
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source MEDLINE; Elektronische Zeitschriftenbibliothek - Frei zugängliche E-Journals
subjects Acid mine drainage
Acid mine water
Acidity
Acids
Analysis methods
Applied sciences
Calcium Carbonate - chemistry
Coal
Coal mines
Coal mining
Dosage
Exact sciences and technology
General purification processes
Gold
Gypsum
Industrial Waste
Iron
Iron - chemistry
Limestone
Mine drainage
Mining
Natural water pollution
Neutralization
Oxidation
Oxygen
Oxygen - chemistry
Pilot plants
Pipes
Pollution
Polyvinyl chloride
Pressure
Removal
Rubber
Scaling
Sludge
Time Factors
Waste Disposal, Fluid - methods
Waste Water - chemistry
Wastewaters
Water
Water Pollutants, Chemical - chemistry
Water treatment and pollution
title Treatment of iron(II)-rich acid mine water with limestone and oxygen
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