Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System
Copper oxide minerals composed of carbonates consume high quantities of leaching reagent. The present research proposes an alternative procedure for malachite leaching (Cu<sub>2</sub>CO<sub>3</sub>(OH)<sub>2</sub>) through the use of only compound, ammonium hydrox...
Main Authors: | , , |
---|---|
Format: | Article |
Language: | English |
Published: |
MDPI AG
2020-06-01
|
Series: | Metals |
Subjects: | |
Online Access: | https://www.mdpi.com/2075-4701/10/6/833 |
id |
doaj-2ed6ceed6d654645bd6746c84aebd71f |
---|---|
record_format |
Article |
spelling |
doaj-2ed6ceed6d654645bd6746c84aebd71f2020-11-25T01:20:26ZengMDPI AGMetals2075-47012020-06-011083383310.3390/met10060833Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH SystemAlvaro Aracena0Javiera Pino1Oscar Jerez2Escuela de Ingeniería Química, Pontificia Universidad Católica de Valparaíso, Avenida Brasil 2162, Valparaíso 2362854, ChileEscuela de Ingeniería Química, Pontificia Universidad Católica de Valparaíso, Avenida Brasil 2162, Valparaíso 2362854, ChileInstituto de Geología Económica Aplicada (GEA), Universidad de Concepción, Casilla 160-C, Concepción 4070386, ChileCopper oxide minerals composed of carbonates consume high quantities of leaching reagent. The present research proposes an alternative procedure for malachite leaching (Cu<sub>2</sub>CO<sub>3</sub>(OH)<sub>2</sub>) through the use of only compound, ammonium hydroxide (NH<sub>4</sub>OH). Preliminary studies were also carried out for the dissolution of malachite in an acid system. The variables evaluated were solution pH, stirring rate, temperature, NH<sub>4</sub>OH concentration, particle size, solid/liquid ratio and different ammonium reagents. The experiments were carried out in a stirred batch system with controlled temperatures and stirring rates. For the acid dissolution system, sulfuric acid consumption reached excessive values (986 kg H<sub>2</sub>SO<sub>4</sub>/ton of malachite), invalidating the dissolution in these common systems. On the other hand, for the ammoniacal system, there was no acid consumption and the results show that copper recovery was very high, reaching values of 84.1% for a concentration of 0.2 mol/dm<sup>3</sup> of NH<sub>4</sub>OH and an experiment time of 7200 s. The theoretical/thermodynamic calculations indicate that the solution pH was a significant factor in maintaining the copper soluble as Cu(NH<sub>3</sub>)<sub>4</sub><sup>2+</sup>. This was validated by the experimental results and solid analysis by X-ray diffraction (XRD), from which the reaction mechanisms were obtained. A heterogeneous kinetic model was obtained from the diffusion model in a porous layer for particles that begin the reaction as nonporous but which become porous during the reaction as the original solid splits and cracks to form a highly porous structure. The reaction order for the NH<sub>4</sub>OH concentration was 3.2 and was inversely proportional to the square of the initial radius of the particle. The activation energy was calculated at 36.1 kJ/mol in the temperature range of 278 to 313 K.https://www.mdpi.com/2075-4701/10/6/833malachitecarbonateleachingammonium hydroxideheterogeneous model |
collection |
DOAJ |
language |
English |
format |
Article |
sources |
DOAJ |
author |
Alvaro Aracena Javiera Pino Oscar Jerez |
spellingShingle |
Alvaro Aracena Javiera Pino Oscar Jerez Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System Metals malachite carbonate leaching ammonium hydroxide heterogeneous model |
author_facet |
Alvaro Aracena Javiera Pino Oscar Jerez |
author_sort |
Alvaro Aracena |
title |
Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System |
title_short |
Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System |
title_full |
Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System |
title_fullStr |
Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System |
title_full_unstemmed |
Mechanism and Kinetics of Malachite Dissolution in an NH<sub>4</sub>OH System |
title_sort |
mechanism and kinetics of malachite dissolution in an nh<sub>4</sub>oh system |
publisher |
MDPI AG |
series |
Metals |
issn |
2075-4701 |
publishDate |
2020-06-01 |
description |
Copper oxide minerals composed of carbonates consume high quantities of leaching reagent. The present research proposes an alternative procedure for malachite leaching (Cu<sub>2</sub>CO<sub>3</sub>(OH)<sub>2</sub>) through the use of only compound, ammonium hydroxide (NH<sub>4</sub>OH). Preliminary studies were also carried out for the dissolution of malachite in an acid system. The variables evaluated were solution pH, stirring rate, temperature, NH<sub>4</sub>OH concentration, particle size, solid/liquid ratio and different ammonium reagents. The experiments were carried out in a stirred batch system with controlled temperatures and stirring rates. For the acid dissolution system, sulfuric acid consumption reached excessive values (986 kg H<sub>2</sub>SO<sub>4</sub>/ton of malachite), invalidating the dissolution in these common systems. On the other hand, for the ammoniacal system, there was no acid consumption and the results show that copper recovery was very high, reaching values of 84.1% for a concentration of 0.2 mol/dm<sup>3</sup> of NH<sub>4</sub>OH and an experiment time of 7200 s. The theoretical/thermodynamic calculations indicate that the solution pH was a significant factor in maintaining the copper soluble as Cu(NH<sub>3</sub>)<sub>4</sub><sup>2+</sup>. This was validated by the experimental results and solid analysis by X-ray diffraction (XRD), from which the reaction mechanisms were obtained. A heterogeneous kinetic model was obtained from the diffusion model in a porous layer for particles that begin the reaction as nonporous but which become porous during the reaction as the original solid splits and cracks to form a highly porous structure. The reaction order for the NH<sub>4</sub>OH concentration was 3.2 and was inversely proportional to the square of the initial radius of the particle. The activation energy was calculated at 36.1 kJ/mol in the temperature range of 278 to 313 K. |
topic |
malachite carbonate leaching ammonium hydroxide heterogeneous model |
url |
https://www.mdpi.com/2075-4701/10/6/833 |
work_keys_str_mv |
AT alvaroaracena mechanismandkineticsofmalachitedissolutioninannhsub4subohsystem AT javierapino mechanismandkineticsofmalachitedissolutioninannhsub4subohsystem AT oscarjerez mechanismandkineticsofmalachitedissolutioninannhsub4subohsystem |
_version_ |
1725134206080647168 |