Abstract
In this work, a physical–chemical activation desilication process was proposed to extract silica from high alumina fly ash (HAFA). The effects of fly ash size, hydrochloric acid concentration, acid activation time, and reaction temperature on the desilication efficiency were investigated comprehensively. The phase and morphology of the original fly ash and desilicated fly ash were analyzed by X-ray diffraction (XRD) and scanning electron microscopy–energy-dispersive X-ray spectroscopy (SEM-EDS). Compared with the traditional desilication process, the physical–chemical activation desilication efficiency is further increased from 38.4% to 53.2% under the optimal conditions. Additionally, the kinetic rules and equations were confirmed by the experimental data fitting with shrinking core model of liquid–solid multiphase reaction. Kinetic studies show that the enhanced desilication process is divided into two processes, and both steps of the two-step reaction is controlled by chemical reaction, and the earlier stage activation energy is 52.05 kJ/mol and the later stage activation energy is 58.45 kJ/mol. The results of mechanism analysis show that physical activation breaks the link between the crystalline phase and the amorphous phase, and then a small amount of alkali-soluble alumina in the amorphous phase is removed by acid activation, thereby suppressing the generation of side reactions of the zeolite phase.
Highlights
High alumina fly ash (HAFA) is a byproduct of high-temperature combustion of high-alumina coal in thermal power plants
Figure shows the effect of physical activation time on the desilication rate, and intensified DHAFA (IDHAFA) under activation conditions
By using physical and chemical activation, the desilication efficiency of HAFA increased from 38.4% to 53.2%
Summary
High alumina fly ash (HAFA) is a byproduct of high-temperature combustion of high-alumina coal in thermal power plants. HAFA contains critical metals such as gallium [4], lithium [5], and rare earths [6,7] that can be extracted in the alumina extraction process as byproducts. Many extraction techniques, such as predesilication soda lime sintering [8], limestone sintering [9], acid leaching [10,11], ammonium sulfate [12] and submolten salt methods [13], have been developed to extract alumina from HAFA. The predesilication soda lime sintering process was carried out at an industrial scale (200 kt per year) by China Datang Corporation in the province of Metals 2019, 9, 411; doi:10.3390/met9040411 www.mdpi.com/journal/metals
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