Kinetic behaviour of the roasting/selective reduction process with the use of a mixture of bituminous coal and fuel oil as the additive

Author:

Angulo-Palma Hugo1ORCID,Saldana Manuel2ORCID,Legrá Ángel3ORCID,Urgellés Alisa4ORCID,Pedrera Carlos5ORCID,Gallegos Sandra6ORCID,Galleguillos Madrid7ORCID,Toro Norman6ORCID

Affiliation:

1. Centro de Investigaciones del Níquel "Alberto Fernández Montes de Oca" (CEDINIQ), Moa, Holguín, Cuba + Departamento de Metalurgia Química, Universidad de Moa, Holguín, Cuba

2. Faculty of Engineering and Architecture, Universidad Arturo Prat, Iquique, Chile + Departamento de Ingeniería Química y Procesos de Minerales, Universidad de Antofagasta, Antofagasta, Chile

3. Centro de Investigaciones del Níquel "Alberto Fernández Montes de Oca2 (CEDINIQ), Moa, Holguín, Cuba

4. Centro de Investigaciones del Níquel "Alberto Fernández Montes de Oca" (CEDINIQ), Moa, Holguín, Cuba

5. Facultad de Ingeniería Química y Agronomía, Universidad de Oriente, Santiago de Cuba, Cuba

6. Faculty of Engineering and Architecture, Universidad Arturo Prat, Iquique, Chile

7. Centro de Desarrollo Energético Antofagasta, Universidad de Antofagasta, Antofagasta, Chile

Abstract

Lateritic ore is currently the main raw material that allows extraction of Ni by the Caron process. To date, the kinetic behaviour of the roasting/selective reduction process of lateritic nickeli-ferous ores on a pilot scale is largely unknown. In the present study, the kinetic behaviour, the controlling stage and the mechanisms that describe this process with the use of a mixture of 2 wt.% bituminous coal and 1.25 wt.% fuel oil as a reducing additive were determined during the evaluation of the high and low thermal profiles, respectively. The phases of the reduced/le-ached minerals and the fed ore were analysed by X-ray powder diffraction. It was observed that the mixture used as a reducing additive guarantees an adequate transformation in both thermal profiles; the relationship between the residual Ni and residence time is described by a first-order reaction with the determination coefficients greater than 0.949. Although the influence of post-combustion air is not analysed, the controlling stage was diffusion through the ash layer with an activation energy of 14.4060 kJ mol-1. Thus, the most precise combination to describe the process is diffusion through the ash layer and the growth of the nuclei.

Publisher

National Library of Serbia

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