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...

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Main Authors: Alvaro Aracena, Javiera Pino, Oscar Jerez
Format: Article
Language:English
Published: MDPI AG 2020-06-01
Series:Metals
Subjects:
Online Access:https://www.mdpi.com/2075-4701/10/6/833
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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
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