dc.contributor.author |
Samouhos, M |
en |
dc.contributor.author |
Hutcheon, R |
en |
dc.contributor.author |
Paspaliaris, I |
en |
dc.date.accessioned |
2014-03-01T01:36:12Z |
|
dc.date.available |
2014-03-01T01:36:12Z |
|
dc.date.issued |
2011 |
en |
dc.identifier.issn |
0892-6875 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/21278 |
|
dc.subject |
Extractive metallurgy |
en |
dc.subject |
Non-metallic ores |
en |
dc.subject |
Pyrometallurgy |
en |
dc.subject |
Reduction |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.subject.classification |
Mineralogy |
en |
dc.subject.classification |
Mining & Mineral Processing |
en |
dc.subject.other |
Carbon content |
en |
dc.subject.other |
Carbon source |
en |
dc.subject.other |
Carbothermic reduction |
en |
dc.subject.other |
Cavity perturbation method |
en |
dc.subject.other |
Copper (ii) |
en |
dc.subject.other |
Dielectric constants |
en |
dc.subject.other |
Energy source |
en |
dc.subject.other |
Experimental procedure |
en |
dc.subject.other |
Graphite powder |
en |
dc.subject.other |
High temperature |
en |
dc.subject.other |
Maximum temperature |
en |
dc.subject.other |
Metallic oxides |
en |
dc.subject.other |
Microwave absorption |
en |
dc.subject.other |
Microwave radiations |
en |
dc.subject.other |
Mineral processing |
en |
dc.subject.other |
Power supply |
en |
dc.subject.other |
Rapid-heating |
en |
dc.subject.other |
Reduction degree |
en |
dc.subject.other |
Reduction rate |
en |
dc.subject.other |
Reduction reaction |
en |
dc.subject.other |
Temperature range |
en |
dc.subject.other |
Time-periods |
en |
dc.subject.other |
Absorption |
en |
dc.subject.other |
Calcination |
en |
dc.subject.other |
Carbothermal reduction |
en |
dc.subject.other |
Copper oxides |
en |
dc.subject.other |
Copper smelting |
en |
dc.subject.other |
Extractive metallurgy |
en |
dc.subject.other |
Froth flotation |
en |
dc.subject.other |
Graphite |
en |
dc.subject.other |
Heating |
en |
dc.subject.other |
Lignite |
en |
dc.subject.other |
Metallic compounds |
en |
dc.subject.other |
Metals |
en |
dc.subject.other |
Microwaves |
en |
dc.subject.other |
Mixtures |
en |
dc.subject.other |
Ores |
en |
dc.subject.other |
Perturbation techniques |
en |
dc.subject.other |
Pyrometallurgy |
en |
dc.subject.other |
Reducing agents |
en |
dc.subject.other |
Carbonate minerals |
en |
dc.title |
Microwave reduction of copper(II) oxide and malachite concentrate |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/j.mineng.2011.03.026 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/j.mineng.2011.03.026 |
en |
heal.language |
English |
en |
heal.publicationDate |
2011 |
en |
heal.abstract |
The use of microwave radiation as an energy source in mineral processing and extractive metallurgy has demonstrated both the instantaneous generation of heat by microwaves in a number of compounds and minerals, and the achievement of high temperatures for an efficient time period enable the heating and reduction of metallic oxides and ores. In the present study, the carbothermic reduction of copper oxide (CuO) and one malachite [Cu2CO3(OH)(2)] concentrate were investigated. To explore feasibility, the dielectric constants [real (epsilon') and imaginary (epsilon '') permittivities] of both materials were measured at the frequencies of 2.45 GHz and 912 MHz, in the temperature range from 25 to 800 degrees C using the cavity perturbation method. The high epsilon '' values (between 1.9 and 36.3) observed in the case of CuO suggest strong microwave absorption, while the malachite concentrate values (between 0.1 and 0.4) indicate limited microwave absorption. Experiments showed the microwave heating rate of CuO was considerably higher than that of the malachite concentrate. The carbothermic reduction of CuO oxide was examined, and the effect of power supply, carbon source, carbon content and granularity of the reducing agent on the reduction rate was studied in detail. Using an 800W power supply, and with addition of lignite as a reducing agent (with carbon content two times stoichiometric), almost complete reduction of 10 g of CuO was achieved in 4 min. The carbothermic reduction of one malachite concentrate was attempted with the same experimental procedure, but the reaction was not possible using only lignite as the reducing agent, since the poor microwave absorption of malachite concentrate-lignite mixture produced a maximum temperature of 200 degrees C. This difficulty was overcome by the addition of 5% by weight of graphite powder to the mixture. The rapid heating of the malachite concentrate-lignite-graphite mixture (800 degrees C after 2 min) resulted in sequential malachite calcination and CuO reduction reactions. After 8 min at a power supply of 800W, the reduction degree of CuO produced by the calcination of malachite was about 90%. (C) 2011 Elsevier Ltd. All rights reserved. |
en |
heal.publisher |
PERGAMON-ELSEVIER SCIENCE LTD |
en |
heal.journalName |
Minerals Engineering |
en |
dc.identifier.doi |
10.1016/j.mineng.2011.03.026 |
en |
dc.identifier.isi |
ISI:000292580800026 |
en |
dc.identifier.volume |
24 |
en |
dc.identifier.issue |
8 |
en |
dc.identifier.spage |
903 |
en |
dc.identifier.epage |
913 |
en |