Biooxidation and precipitation for iron and sulfate removal from heap bioleaching effluent streams

Pauliina Nurmi, Bestamin Özkaya, Keiko Sasaki, Anna H. Kaksonen, Marja Riekkola-Vanhanen, Olli H. Tuovinen, Jaakko A. Puhakka

研究成果: ジャーナルへの寄稿記事

28 引用 (Scopus)

抄録

Effluents from bioleaching processes cause severe problems if dispersed in the environment since they typically have very low pH values and high sulfate and ferric iron concentrations. Dissolved iron may also interfere with the metal recovery. In the bioleaching circuit, partial removal of dissolved iron and sulfate is needed to alleviate process disturbances. In this study, an integrated, bench-scale process comprising a fluidized-bed reactor (FBR) and a gravity settler was developed for controlled biological oxidation of ferrous iron and precipitative removal of ferric iron and sulfate for use in waste management of heap bioleaching processes. The FBR for iron oxidation by an enrichment culture dominated by Leptospirillum ferriphilum was operated at 37 ± 2 °C. The FBR recycle liquor was partially neutralized with 10 M KOH or 50 g/L CaCO 3 slurry to promote ferric iron and sulfate precipitation. With 6 ± 1.5 g Fe 2+ /L in the feed and KOH-adjusted pH 3.5, the oxidation rate of Fe 2+ was 3.7 g/L h and 99% precipitation of ferric iron was achieved in the process. Adjustment with CaCO 3 to pH 3.2 slightly decreased the oxidation rate to 3.3 g/L h and 98% of ferric iron precipitated. With 15 g Fe 2+ /L in the feed, the oxidation rate was 7.0 g Fe 2+ /L h coupled with 96% precipitation of ferric iron. A solid solution of jarosite was the main product of ferric iron precipitation with KOH adjustment and with minor amounts of goethite at the higher pH range. Adjustment of the pH with CaCO 3 precipitated ferric iron also as a solid solution of jarosite, and sulfate precipitated also in the form of gypsum (CaSO 4 ·2H 2 O) especially at the higher pH values.

元の言語英語
ページ(範囲)7-14
ページ数8
ジャーナルHydrometallurgy
101
発行部数1-2
DOI
出版物ステータス出版済み - 2 1 2010

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Bioleaching
Sulfates
Effluents
Iron
Oxidation
Fluidized beds
Solid solutions
Metal recovery
Calcium Sulfate
Gypsum
Waste management
Gravitation

All Science Journal Classification (ASJC) codes

  • Industrial and Manufacturing Engineering
  • Metals and Alloys
  • Materials Chemistry

これを引用

Nurmi, P., Özkaya, B., Sasaki, K., Kaksonen, A. H., Riekkola-Vanhanen, M., Tuovinen, O. H., & Puhakka, J. A. (2010). Biooxidation and precipitation for iron and sulfate removal from heap bioleaching effluent streams. Hydrometallurgy, 101(1-2), 7-14. https://doi.org/10.1016/j.hydromet.2009.11.004

Biooxidation and precipitation for iron and sulfate removal from heap bioleaching effluent streams. / Nurmi, Pauliina; Özkaya, Bestamin; Sasaki, Keiko; Kaksonen, Anna H.; Riekkola-Vanhanen, Marja; Tuovinen, Olli H.; Puhakka, Jaakko A.

:: Hydrometallurgy, 巻 101, 番号 1-2, 01.02.2010, p. 7-14.

研究成果: ジャーナルへの寄稿記事

Nurmi, P, Özkaya, B, Sasaki, K, Kaksonen, AH, Riekkola-Vanhanen, M, Tuovinen, OH & Puhakka, JA 2010, 'Biooxidation and precipitation for iron and sulfate removal from heap bioleaching effluent streams', Hydrometallurgy, 巻. 101, 番号 1-2, pp. 7-14. https://doi.org/10.1016/j.hydromet.2009.11.004
Nurmi, Pauliina ; Özkaya, Bestamin ; Sasaki, Keiko ; Kaksonen, Anna H. ; Riekkola-Vanhanen, Marja ; Tuovinen, Olli H. ; Puhakka, Jaakko A. / Biooxidation and precipitation for iron and sulfate removal from heap bioleaching effluent streams. :: Hydrometallurgy. 2010 ; 巻 101, 番号 1-2. pp. 7-14.
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abstract = "Effluents from bioleaching processes cause severe problems if dispersed in the environment since they typically have very low pH values and high sulfate and ferric iron concentrations. Dissolved iron may also interfere with the metal recovery. In the bioleaching circuit, partial removal of dissolved iron and sulfate is needed to alleviate process disturbances. In this study, an integrated, bench-scale process comprising a fluidized-bed reactor (FBR) and a gravity settler was developed for controlled biological oxidation of ferrous iron and precipitative removal of ferric iron and sulfate for use in waste management of heap bioleaching processes. The FBR for iron oxidation by an enrichment culture dominated by Leptospirillum ferriphilum was operated at 37 ± 2 °C. The FBR recycle liquor was partially neutralized with 10 M KOH or 50 g/L CaCO 3 slurry to promote ferric iron and sulfate precipitation. With 6 ± 1.5 g Fe 2+ /L in the feed and KOH-adjusted pH 3.5, the oxidation rate of Fe 2+ was 3.7 g/L h and 99{\%} precipitation of ferric iron was achieved in the process. Adjustment with CaCO 3 to pH 3.2 slightly decreased the oxidation rate to 3.3 g/L h and 98{\%} of ferric iron precipitated. With 15 g Fe 2+ /L in the feed, the oxidation rate was 7.0 g Fe 2+ /L h coupled with 96{\%} precipitation of ferric iron. A solid solution of jarosite was the main product of ferric iron precipitation with KOH adjustment and with minor amounts of goethite at the higher pH range. Adjustment of the pH with CaCO 3 precipitated ferric iron also as a solid solution of jarosite, and sulfate precipitated also in the form of gypsum (CaSO 4 ·2H 2 O) especially at the higher pH values.",
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AU - Sasaki, Keiko

AU - Kaksonen, Anna H.

AU - Riekkola-Vanhanen, Marja

AU - Tuovinen, Olli H.

AU - Puhakka, Jaakko A.

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