Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution
Harbor sediments contaminated with ZnS concentrate were treated by ferric chloride in HCl solution to remove Zn. The sediments were evaluated using Tessier’s sequential extraction method to determine the different metal phase associations of Zn. Leaching tests were performed to investigate the effec...
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doaj-687ed756f1724a85a8b505a046dcd8332020-11-24T23:39:25ZengMDPI AGMetals2075-47012015-10-01541812182010.3390/met5041812met5041812Removal of Zn from Contaminated Sediment by FeCl3 in HCl SolutionSang-hun Lee0Ohhyeok Kwon1Kyoungkeun Yoo2Richard Diaz Alorro3Gas & Mining Plant Division, Samsung Construction & Technology, Seoul 137-956, KoreaDepartment of Energy & Resources Engineering, Korea Maritime and Ocean University (KMOU), Busan 606-791, KoreaDepartment of Energy & Resources Engineering, Korea Maritime and Ocean University (KMOU), Busan 606-791, KoreaDepartment of Mining Engineering and Metallurgical Engineering, Western Australian School of Mines, Curtin University, Kalgoorlie, WA 6430, AustraliaHarbor sediments contaminated with ZnS concentrate were treated by ferric chloride in HCl solution to remove Zn. The sediments were evaluated using Tessier’s sequential extraction method to determine the different metal phase associations of Zn. Leaching tests were performed to investigate the effects of experimental factors, such as agitation speed, ferric ion concentration, temperature, and pulp density, on the removal of Zn. The sequential extraction procedure revealed that about 17.7% of Zn in the sediment was associated with soluble carbonate and oxide phases. The results of the leaching tests indicated that higher ferric concentration and temperature increased the leaching efficiencies significantly, while the agitation speed has a negligible effect on the removal of Zn. The removal ratio increased to more than 99% within 120 min of treatment at 1 kmol·m−3 HCl solution with 1 kmol·m−3 Fe3+, 10% pulp density, and 400 rpm at 90 °C. The dissolution kinetics of Zn were discussed by comparing the two shrinking core models. It was determined that the kinetic data followed the diffusion controlled model well compared to the surface chemical reaction model. The activation energies were calculated to be 76.9 kJ/mol, 69.6 kJ/mol, and 58.5 kJ/mol for 0.25 kmol·m−3, 0.5 kmol·m−3, and 1 kmol·m−3 Fe3+, respectively.http://www.mdpi.com/2075-4701/5/4/1812harbor sedimentsferric chloridezinc sulfidemetal contamination |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Sang-hun Lee Ohhyeok Kwon Kyoungkeun Yoo Richard Diaz Alorro |
spellingShingle |
Sang-hun Lee Ohhyeok Kwon Kyoungkeun Yoo Richard Diaz Alorro Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution Metals harbor sediments ferric chloride zinc sulfide metal contamination |
author_facet |
Sang-hun Lee Ohhyeok Kwon Kyoungkeun Yoo Richard Diaz Alorro |
author_sort |
Sang-hun Lee |
title |
Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution |
title_short |
Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution |
title_full |
Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution |
title_fullStr |
Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution |
title_full_unstemmed |
Removal of Zn from Contaminated Sediment by FeCl3 in HCl Solution |
title_sort |
removal of zn from contaminated sediment by fecl3 in hcl solution |
publisher |
MDPI AG |
series |
Metals |
issn |
2075-4701 |
publishDate |
2015-10-01 |
description |
Harbor sediments contaminated with ZnS concentrate were treated by ferric chloride in HCl solution to remove Zn. The sediments were evaluated using Tessier’s sequential extraction method to determine the different metal phase associations of Zn. Leaching tests were performed to investigate the effects of experimental factors, such as agitation speed, ferric ion concentration, temperature, and pulp density, on the removal of Zn. The sequential extraction procedure revealed that about 17.7% of Zn in the sediment was associated with soluble carbonate and oxide phases. The results of the leaching tests indicated that higher ferric concentration and temperature increased the leaching efficiencies significantly, while the agitation speed has a negligible effect on the removal of Zn. The removal ratio increased to more than 99% within 120 min of treatment at 1 kmol·m−3 HCl solution with 1 kmol·m−3 Fe3+, 10% pulp density, and 400 rpm at 90 °C. The dissolution kinetics of Zn were discussed by comparing the two shrinking core models. It was determined that the kinetic data followed the diffusion controlled model well compared to the surface chemical reaction model. The activation energies were calculated to be 76.9 kJ/mol, 69.6 kJ/mol, and 58.5 kJ/mol for 0.25 kmol·m−3, 0.5 kmol·m−3, and 1 kmol·m−3 Fe3+, respectively. |
topic |
harbor sediments ferric chloride zinc sulfide metal contamination |
url |
http://www.mdpi.com/2075-4701/5/4/1812 |
work_keys_str_mv |
AT sanghunlee removalofznfromcontaminatedsedimentbyfecl3inhclsolution AT ohhyeokkwon removalofznfromcontaminatedsedimentbyfecl3inhclsolution AT kyoungkeunyoo removalofznfromcontaminatedsedimentbyfecl3inhclsolution AT richarddiazalorro removalofznfromcontaminatedsedimentbyfecl3inhclsolution |
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