Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone
Limestones and their modifications from Nordkalk Corporation (Finland) flotation fines (FF) and filter sand (FS) as potential adsorbents for AMD treatment and wastewater purification from Cu, Fe, Zn and Ni ions were studied. Limestones were capable of binding significant amounts of Cu and Fe from sy...
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Online Access: | https://hdl.handle.net/20.500.11937/20682 https://doi.org/10.1016/j.ecoleng.2015.04.046 |
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ftcurtin:oai:espace.curtin.edu.au:20.500.11937/20682 2023-06-11T04:14:14+02:00 Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone Iakovleva, E. Mäkilä, E. Salonen, J. Sitarz, M. Wang, Shaobin Sillanpää, M. 2014 restricted https://hdl.handle.net/20.500.11937/20682 https://doi.org/10.1016/j.ecoleng.2015.04.046 unknown Elsevier http://hdl.handle.net/20.500.11937/20682 doi:10.1016/j.ecoleng.2015.04.046 Journal Article 2014 ftcurtin https://doi.org/20.500.11937/2068210.1016/j.ecoleng.2015.04.046 2023-05-30T19:30:47Z Limestones and their modifications from Nordkalk Corporation (Finland) flotation fines (FF) and filter sand (FS) as potential adsorbents for AMD treatment and wastewater purification from Cu, Fe, Zn and Ni ions were studied. Limestones were capable of binding significant amounts of Cu and Fe from synthetic AMD solutions and wastewater, while unmodified limestones were not good for Zn and Ni removal. Two methods of surface area modification were suggested. The first one with 2 M solution of NaCl and the second one with wastewater from Norilsk Nickel Harjavalta. The structure of materials and their surface area were characterized by SEM, EDX, MIR spectroscopy and nitrogen adsorption methods. Optimal amount of adsorbents for different model and real solutions was found. Adsorption kinetics showed that the adsorption equilibrium was reached within approximately 8 h. The kinetic data fits to a pseudo second order model with correlation coefficients greater than 0.999. The adsorption capacity was the highest at solution pH range of 6–7. Langmuir, Toth and Sips models were used to fit the adsorption isotherms. Based on the parameters calculated from models, the adsorption capacity decreased in the order of Cu > Fe > Zn > Ni for FF and Fe > Cu > Zn > Ni for FS. The research showed that the proposed modified limestones can be successfully used for AMD neutralization and removal of Cu(II), Fe(III), Zn(II) and Ni(II). Article in Journal/Newspaper norilsk Curtin University: espace Langmuir ENVELOPE(-67.150,-67.150,-66.967,-66.967) Norilsk ENVELOPE(88.203,88.203,69.354,69.354) Toth ENVELOPE(-155.250,-155.250,-86.367,-86.367) Ecological Engineering 81 30 40 |
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Curtin University: espace |
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language |
unknown |
description |
Limestones and their modifications from Nordkalk Corporation (Finland) flotation fines (FF) and filter sand (FS) as potential adsorbents for AMD treatment and wastewater purification from Cu, Fe, Zn and Ni ions were studied. Limestones were capable of binding significant amounts of Cu and Fe from synthetic AMD solutions and wastewater, while unmodified limestones were not good for Zn and Ni removal. Two methods of surface area modification were suggested. The first one with 2 M solution of NaCl and the second one with wastewater from Norilsk Nickel Harjavalta. The structure of materials and their surface area were characterized by SEM, EDX, MIR spectroscopy and nitrogen adsorption methods. Optimal amount of adsorbents for different model and real solutions was found. Adsorption kinetics showed that the adsorption equilibrium was reached within approximately 8 h. The kinetic data fits to a pseudo second order model with correlation coefficients greater than 0.999. The adsorption capacity was the highest at solution pH range of 6–7. Langmuir, Toth and Sips models were used to fit the adsorption isotherms. Based on the parameters calculated from models, the adsorption capacity decreased in the order of Cu > Fe > Zn > Ni for FF and Fe > Cu > Zn > Ni for FS. The research showed that the proposed modified limestones can be successfully used for AMD neutralization and removal of Cu(II), Fe(III), Zn(II) and Ni(II). |
format |
Article in Journal/Newspaper |
author |
Iakovleva, E. Mäkilä, E. Salonen, J. Sitarz, M. Wang, Shaobin Sillanpää, M. |
spellingShingle |
Iakovleva, E. Mäkilä, E. Salonen, J. Sitarz, M. Wang, Shaobin Sillanpää, M. Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
author_facet |
Iakovleva, E. Mäkilä, E. Salonen, J. Sitarz, M. Wang, Shaobin Sillanpää, M. |
author_sort |
Iakovleva, E. |
title |
Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
title_short |
Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
title_full |
Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
title_fullStr |
Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
title_full_unstemmed |
Acid mine drainage (AMD) treatment: Neutralization and toxic elements removal with unmodified and modified limestone |
title_sort |
acid mine drainage (amd) treatment: neutralization and toxic elements removal with unmodified and modified limestone |
publisher |
Elsevier |
publishDate |
2014 |
url |
https://hdl.handle.net/20.500.11937/20682 https://doi.org/10.1016/j.ecoleng.2015.04.046 |
long_lat |
ENVELOPE(-67.150,-67.150,-66.967,-66.967) ENVELOPE(88.203,88.203,69.354,69.354) ENVELOPE(-155.250,-155.250,-86.367,-86.367) |
geographic |
Langmuir Norilsk Toth |
geographic_facet |
Langmuir Norilsk Toth |
genre |
norilsk |
genre_facet |
norilsk |
op_relation |
http://hdl.handle.net/20.500.11937/20682 doi:10.1016/j.ecoleng.2015.04.046 |
op_doi |
https://doi.org/20.500.11937/2068210.1016/j.ecoleng.2015.04.046 |
container_title |
Ecological Engineering |
container_volume |
81 |
container_start_page |
30 |
op_container_end_page |
40 |
_version_ |
1768392102930022400 |