TY - JOUR
T1 - Magnesium recovery from ferronickel slag by reaction with sodium hydroxide
AU - Abdul, Fakhreza
AU - Adachi, Ken
AU - Ho, Hsing Jung
AU - Iizuka, Atsushi
AU - Shibata, Etsuro
N1 - Publisher Copyright:
© 2024 The Authors
PY - 2024/6
Y1 - 2024/6
N2 - Ferronickel (FeNi) slag, as the main solid byproduct of the FeNi industry, has the potential to be utilized other than as roadbed material. To broaden the applications of FeNi slag (such as CO2-capturing materials), there is a need for a treatment that breaks the magnesium silicate bonds and transforms the magnesium into MgO. As an initial study, this research treated FeNi slag by using sodium hydroxide followed by water-washing. The present authors evaluated several alkali treatment variables; such as temperature (523 K and 773 K), time (1–8 h), and mass ratio between FeNi slag and NaOH (1:0.75–1:4). The magnesium in FeNi slag was recovered as MgO. By using a FeNi slag:NaOH mass ratio of 1:2, a temperature of 773 K, and a time of 4 h, 97.34% of the magnesium was recovered, and 83.35% of the silicon was removed. During alkali treatment, the Mg-based compound in FeNi slag undergoes a transformation from MgSiO3 to Mg2SiO4 to MgNa2SiO4 and, finally, to MgO. On the other hand, the Fe-based compound transforms olivine to Fe2O3 to spinel (Fe2MgO4 and Fe3O4) and, finally, to FeNaO2. The alkali treatment process of FeNi slag using NaOH followed by water washing is also known to make the product morphology porous and has a large surface area (11.62 m2/g). In terms of economics, this process will be economical when considering the by-product (Na4SiO4) generated.
AB - Ferronickel (FeNi) slag, as the main solid byproduct of the FeNi industry, has the potential to be utilized other than as roadbed material. To broaden the applications of FeNi slag (such as CO2-capturing materials), there is a need for a treatment that breaks the magnesium silicate bonds and transforms the magnesium into MgO. As an initial study, this research treated FeNi slag by using sodium hydroxide followed by water-washing. The present authors evaluated several alkali treatment variables; such as temperature (523 K and 773 K), time (1–8 h), and mass ratio between FeNi slag and NaOH (1:0.75–1:4). The magnesium in FeNi slag was recovered as MgO. By using a FeNi slag:NaOH mass ratio of 1:2, a temperature of 773 K, and a time of 4 h, 97.34% of the magnesium was recovered, and 83.35% of the silicon was removed. During alkali treatment, the Mg-based compound in FeNi slag undergoes a transformation from MgSiO3 to Mg2SiO4 to MgNa2SiO4 and, finally, to MgO. On the other hand, the Fe-based compound transforms olivine to Fe2O3 to spinel (Fe2MgO4 and Fe3O4) and, finally, to FeNaO2. The alkali treatment process of FeNi slag using NaOH followed by water washing is also known to make the product morphology porous and has a large surface area (11.62 m2/g). In terms of economics, this process will be economical when considering the by-product (Na4SiO4) generated.
KW - Alkali fusion
KW - Ferronickel slag
KW - Magnesium oxide recovery
KW - Solid–solid reaction
KW - Waste utilization
UR - http://www.scopus.com/inward/record.url?scp=85188738125&partnerID=8YFLogxK
U2 - 10.1016/j.jece.2024.112516
DO - 10.1016/j.jece.2024.112516
M3 - Article
AN - SCOPUS:85188738125
SN - 2213-2929
VL - 12
JO - Journal of Environmental Chemical Engineering
JF - Journal of Environmental Chemical Engineering
IS - 3
M1 - 112516
ER -