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Extraction of alumina and silica from high-silica bauxite by sintering with sodium carbonate followed by two-step leaching with water and sulfuric acid

Efficient utilization of high-silica bauxite and minimization of bauxite residue are of great significance for the sustainable development of the alumina industry. In this paper, a novel process is proposed to extract Al(2)O(3) and SiO(2) from high-silica bauxite without residue discharge, that is,...

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Detalles Bibliográficos
Autores principales: Sun, Yue, Pan, Aifang, Ma, Yuzhao, Chang, Jie
Formato: Online Artículo Texto
Lenguaje:English
Publicado: The Royal Society of Chemistry 2023
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC10394738/
https://www.ncbi.nlm.nih.gov/pubmed/37538514
http://dx.doi.org/10.1039/d3ra03362g
Descripción
Sumario:Efficient utilization of high-silica bauxite and minimization of bauxite residue are of great significance for the sustainable development of the alumina industry. In this paper, a novel process is proposed to extract Al(2)O(3) and SiO(2) from high-silica bauxite without residue discharge, that is, sintering bauxite with Na(2)CO(3) followed by two-step leaching with water and sulfuric acid. The effects of the sintering parameters on the process were investigated, and the phase transformations during sintering and leaching were revealed by using phase diagram, thermogravimetric analysis (TGA) and differential scanning calorimetric (DSC), X-ray diffraction (XRD), scanning electron microscopy (SEM) and energy dispersive spectrometer (EDS) methods. When the mixture of the high-silica bauxite and Na(2)CO(3) with mole ratio of Na(2)O/(Al(2)O(3) + SiO(2)) of 1 was sintered at 950 °C for 30 min, diaspore and kaolinite were primarily converted into Na(1.95)Al(1.95)Si(0.05)O(4) and an amorphous phase, respectively. In the water leaching process, Na(1.95)Al(1.95)Si(0.05)O(4) was dissolved while the amorphous phase underwent some transformations to form the water leaching residue, resulting in ∼84% of Al(2)O(3) being extracted for alumina production. In the sulfuric acid leaching process, the amorphous phase in the water leaching residue dissolved, resulting in ∼13% of Al(2)O(3) and ∼86% of SiO(2) being extracted for the production of polyaluminium ferric sulfate (PAFS) and silica gel, respectively. The silica gel had a high purity, containing more than 88% of SiO(2) after drying.