TY - JOUR
T1 - Nickel recovery in ferronickel concentrate by green selective reduction of nickel laterite
AU - Sari, Yuliana
AU - Manaf, Azwar
AU - Astuti, Widi
AU - Nurjaman, Fajar
AU - Susanti, Diah
AU - Sipahutar, Wahyu Solafide
AU - Bahfie, Fathan
N1 - Publisher Copyright:
© 2024 THE AUTHORS
PY - 2024/9
Y1 - 2024/9
N2 - Nickel laterite is typically processed into ferronickel through a pyrometallurgical method involving high temperatures and the use of fossil fuels, such as coals or cokes. Unfortunately, this process releases emissions like CO2, SO2, and NOx into the environment. This study explores a sustainable approach for nickel laterite processing by investigating low-temperature selective reduction using various biomass reductants. The materials, including saprolitic nickel ore and biomass types (palm kernel shell charcoal or PSC, lamtoro wood charcoal, coconut shell charcoal, and rubber wood charcoal), undergo pelletization, selective reduction at 1150 °C, and wet magnetic separation. PSC biomass is superior to other biomass due to its 217.2 m2/g specific surface area value. Optimal conditions were achieved using 0.3 stoichiometric PSC, along with the addition of 10 wt% of sodium sulfate as an additive. This has led to a nickel mass fraction of 26.0 wt% and a recovery rate of 27.4 %.
AB - Nickel laterite is typically processed into ferronickel through a pyrometallurgical method involving high temperatures and the use of fossil fuels, such as coals or cokes. Unfortunately, this process releases emissions like CO2, SO2, and NOx into the environment. This study explores a sustainable approach for nickel laterite processing by investigating low-temperature selective reduction using various biomass reductants. The materials, including saprolitic nickel ore and biomass types (palm kernel shell charcoal or PSC, lamtoro wood charcoal, coconut shell charcoal, and rubber wood charcoal), undergo pelletization, selective reduction at 1150 °C, and wet magnetic separation. PSC biomass is superior to other biomass due to its 217.2 m2/g specific surface area value. Optimal conditions were achieved using 0.3 stoichiometric PSC, along with the addition of 10 wt% of sodium sulfate as an additive. This has led to a nickel mass fraction of 26.0 wt% and a recovery rate of 27.4 %.
KW - Biomass reductant
KW - Ferronickel
KW - Nickel laterite ore
KW - Selective reduction
UR - http://www.scopus.com/inward/record.url?scp=85201492811&partnerID=8YFLogxK
U2 - 10.1016/j.jestch.2024.101798
DO - 10.1016/j.jestch.2024.101798
M3 - Article
AN - SCOPUS:85201492811
SN - 2215-0986
VL - 57
JO - Engineering Science and Technology, an International Journal
JF - Engineering Science and Technology, an International Journal
M1 - 101798
ER -