dc.contributor.author |
Tsakiridis, PE |
en |
dc.contributor.author |
Oustadakis, P |
en |
dc.contributor.author |
Katsiapi, A |
en |
dc.contributor.author |
Agatzini-Leonardou, S |
en |
dc.date.accessioned |
2014-03-01T01:33:37Z |
|
dc.date.available |
2014-03-01T01:33:37Z |
|
dc.date.issued |
2010 |
en |
dc.identifier.issn |
0304-3894 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/20490 |
|
dc.subject |
EAFD |
en |
dc.subject |
Electrowinning |
en |
dc.subject |
Leach liquor |
en |
dc.subject |
Purification |
en |
dc.subject.classification |
Engineering, Environmental |
en |
dc.subject.classification |
Engineering, Civil |
en |
dc.subject.classification |
Environmental Sciences |
en |
dc.subject.other |
Agitation leaching |
en |
dc.subject.other |
Chemical precipitation |
en |
dc.subject.other |
Cyanex 272 |
en |
dc.subject.other |
Downstream-processing |
en |
dc.subject.other |
Electric arc furnace dust |
en |
dc.subject.other |
Extractant concentration |
en |
dc.subject.other |
High-purity |
en |
dc.subject.other |
Hydrometallurgical process |
en |
dc.subject.other |
Jarosites |
en |
dc.subject.other |
Leach liquor |
en |
dc.subject.other |
Leach liquors |
en |
dc.subject.other |
Organic phase |
en |
dc.subject.other |
Purification process |
en |
dc.subject.other |
Spent electrolytes |
en |
dc.subject.other |
Sulphate solutions |
en |
dc.subject.other |
Sulphates |
en |
dc.subject.other |
Sulphuric acids |
en |
dc.subject.other |
Unit operation |
en |
dc.subject.other |
Zinc electrowinning |
en |
dc.subject.other |
Zinc recovery |
en |
dc.subject.other |
Atmospheric pressure |
en |
dc.subject.other |
Cavity resonators |
en |
dc.subject.other |
Dust control |
en |
dc.subject.other |
Electric arcs |
en |
dc.subject.other |
Electric furnace process |
en |
dc.subject.other |
Electric furnaces |
en |
dc.subject.other |
Electrolytes |
en |
dc.subject.other |
Electrowinning |
en |
dc.subject.other |
Furnaces |
en |
dc.subject.other |
Hydrometallurgy |
en |
dc.subject.other |
Leaching |
en |
dc.subject.other |
Lead |
en |
dc.subject.other |
Metal recovery |
en |
dc.subject.other |
Purification |
en |
dc.subject.other |
Salt removal |
en |
dc.subject.other |
Solvent extraction |
en |
dc.subject.other |
Solvents |
en |
dc.subject.other |
Steel metallurgy |
en |
dc.subject.other |
Stripping (dyes) |
en |
dc.subject.other |
Sulfuric acid |
en |
dc.subject.other |
Zinc metallurgy |
en |
dc.subject.other |
Zinc |
en |
dc.subject.other |
iron |
en |
dc.subject.other |
sulfate |
en |
dc.subject.other |
zinc |
en |
dc.subject.other |
acidity |
en |
dc.subject.other |
aqueous solution |
en |
dc.subject.other |
dust |
en |
dc.subject.other |
electrokinesis |
en |
dc.subject.other |
electrolyte |
en |
dc.subject.other |
extraction method |
en |
dc.subject.other |
ion exchange |
en |
dc.subject.other |
leaching |
en |
dc.subject.other |
metallurgy |
en |
dc.subject.other |
pH |
en |
dc.subject.other |
precipitation (chemistry) |
en |
dc.subject.other |
processing |
en |
dc.subject.other |
solvent |
en |
dc.subject.other |
sulfuric acid |
en |
dc.subject.other |
acidity |
en |
dc.subject.other |
article |
en |
dc.subject.other |
downstream processing |
en |
dc.subject.other |
dust |
en |
dc.subject.other |
electrowinning |
en |
dc.subject.other |
industrial waste |
en |
dc.subject.other |
iron and steel industry |
en |
dc.subject.other |
leaching |
en |
dc.subject.other |
metallurgy |
en |
dc.subject.other |
purification |
en |
dc.subject.other |
waste component removal |
en |
dc.subject.other |
Dust |
en |
dc.subject.other |
Electrochemistry |
en |
dc.subject.other |
Electrolytes |
en |
dc.subject.other |
Indicators and Reagents |
en |
dc.subject.other |
Iron |
en |
dc.subject.other |
Metallurgy |
en |
dc.subject.other |
Microscopy, Electron, Scanning |
en |
dc.subject.other |
Phosphinic Acids |
en |
dc.subject.other |
Solvents |
en |
dc.subject.other |
X-Ray Diffraction |
en |
dc.subject.other |
Zinc |
en |
dc.title |
Hydrometallurgical process for zinc recovery from electric arc furnace dust (EAFD). Part II: Downstream processing and zinc recovery by electrowinning |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/j.jhazmat.2010.04.004 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/j.jhazmat.2010.04.004 |
en |
heal.language |
English |
en |
heal.publicationDate |
2010 |
en |
heal.abstract |
The characterization and the agitation leaching of electric arc furnace dust (EAFD) by diluted sulphuric acid have been studied in Part I, as a separate article. The aim of the present research work (Part II) is the development of a purification process of the leach liquor for the recovery of high-purity zinc by electrowinning. The proposed hydrometallurgical process consists of the following four (4) unit operations: (1) Removal of iron as easily filterable crystalline basic sulphate salt of the jarosite type, at atmospheric pressure, by chemical precipitation at pH: 3.5 and 95 degrees C. (2) Zinc solvent extraction by Cyanex 272 at pH: 3.5, T: 40 degrees C, with 25% extractant concentration. (3) Stripping of the loaded organic phase by zinc spent electrolyte (62.5 g/L Zn2+) at T: 40 degrees C with diluted H2SO4 (3 mol/L). (4) Zinc electrowinning from sulphate solutions (at 38 degrees C) using Al as cathode and Pb as anode. The acidity of the electrolyte was fixed at 180 g/L H2SO4, while the current density was kept constant at 500 A/m(2). (C) 2010 Elsevier B.V. All rights reserved. |
en |
heal.publisher |
ELSEVIER SCIENCE BV |
en |
heal.journalName |
Journal of Hazardous Materials |
en |
dc.identifier.doi |
10.1016/j.jhazmat.2010.04.004 |
en |
dc.identifier.isi |
ISI:000278626700002 |
en |
dc.identifier.volume |
179 |
en |
dc.identifier.issue |
1-3 |
en |
dc.identifier.spage |
8 |
en |
dc.identifier.epage |
14 |
en |