TY - JOUR
T1 - Exploration of biomass ashes (BA) to decontaminate highly metal-rich acid mine drainages (AMDs)
T2 - Column and batch experiments
AU - Cánovas, Carlos Ruiz
AU - Amaya-Yaeggy, Gerardo A.
AU - Kotte Hewa, Dileesha Jayahansani
AU - Pérez-López, Rafael
AU - Macías, Francisco
AU - León, Rafael
AU - Nieto, José Miguel
AU - Basallote, María Dolores
N1 - Score=10
Publisher Copyright:
© 2025 Elsevier Ltd
PY - 2025/1/15
Y1 - 2025/1/15
N2 - This work investigates the suitability of biomass ash (BA), a waste generated after biomass burning, as alkaline material to treat highly acidic (pH 1.9–2.0) and metal rich acid mine drainages (AMD). To address this issue, batch (at solid:liquid ratios of 1:2, 1:5; 1:10, 1:20, 1:100 and 1:200) and column experiments were performed. During batch experiments, the contact of AMD with BA provoked an intense increase of pH values, especially at higher S:L ratios (1:2 and 1:5), i.e., from 1.9 to 7.3 and 6.4, respectively, due to the alkalinity provided by BA, which led to strong removal of dissolved metal/loids (e.g., 89–99 % of Fe, 99% of Al, Cu and As, 75–99% of Pb) and sulfate (66–68%) for both ratios. The removal efficiency obtained using intermediate and low S:L ratios was remarkably lower for most metal/loids except for As, with values above 95% at the end of the experiment for all S:L ratios. On the other hand, the dissolution of metal oxides, initially contained in BA, led to the release of elements commonly found associated to these oxides in BA (e.g., Al, Ca, Mg, K, Na, Sr, or P). The removal rates obtained in column experiments were lower, due to the fast depletion of alkalinity during the first days of the experiment, which make columns less suitable for AMD treatment than batch reactors. A removal of 100% of Cu, As, V and Ga, 99% of Pb, 73% of Fe and Cd, 64% of Zn and Co, and 60% of sulfate was achieved after 24 h. However, the efficiency of the column decreased progressively to the end of the experiment, reaching similar values than in input waters, except in the case of As (around 91% of removal), due to the preferential sorption of oxyanions (H2AsO4− and HAsO42−). The precipitation of schwertmannite and to a lesser extent jarosite, and sorption processes on these minerals, are the main process controlling metal retention in both batch and column experiments. Despite the low alkalinity of the BA used, the removal rates of metal (loid)s were significant, and hence, it constitutes a promising option to treat AMD in mining areas worldwide where this waste is generated.
AB - This work investigates the suitability of biomass ash (BA), a waste generated after biomass burning, as alkaline material to treat highly acidic (pH 1.9–2.0) and metal rich acid mine drainages (AMD). To address this issue, batch (at solid:liquid ratios of 1:2, 1:5; 1:10, 1:20, 1:100 and 1:200) and column experiments were performed. During batch experiments, the contact of AMD with BA provoked an intense increase of pH values, especially at higher S:L ratios (1:2 and 1:5), i.e., from 1.9 to 7.3 and 6.4, respectively, due to the alkalinity provided by BA, which led to strong removal of dissolved metal/loids (e.g., 89–99 % of Fe, 99% of Al, Cu and As, 75–99% of Pb) and sulfate (66–68%) for both ratios. The removal efficiency obtained using intermediate and low S:L ratios was remarkably lower for most metal/loids except for As, with values above 95% at the end of the experiment for all S:L ratios. On the other hand, the dissolution of metal oxides, initially contained in BA, led to the release of elements commonly found associated to these oxides in BA (e.g., Al, Ca, Mg, K, Na, Sr, or P). The removal rates obtained in column experiments were lower, due to the fast depletion of alkalinity during the first days of the experiment, which make columns less suitable for AMD treatment than batch reactors. A removal of 100% of Cu, As, V and Ga, 99% of Pb, 73% of Fe and Cd, 64% of Zn and Co, and 60% of sulfate was achieved after 24 h. However, the efficiency of the column decreased progressively to the end of the experiment, reaching similar values than in input waters, except in the case of As (around 91% of removal), due to the preferential sorption of oxyanions (H2AsO4− and HAsO42−). The precipitation of schwertmannite and to a lesser extent jarosite, and sorption processes on these minerals, are the main process controlling metal retention in both batch and column experiments. Despite the low alkalinity of the BA used, the removal rates of metal (loid)s were significant, and hence, it constitutes a promising option to treat AMD in mining areas worldwide where this waste is generated.
KW - Acid mine drainage
KW - Active treatment
KW - Biomass ashes
KW - Circular economy
KW - Passive treatment
UR - http://www.scopus.com/inward/record.url?scp=85214324167&partnerID=8YFLogxK
U2 - 10.1016/j.jclepro.2025.144679
DO - 10.1016/j.jclepro.2025.144679
M3 - Article
AN - SCOPUS:85214324167
SN - 0959-6526
VL - 489
JO - Journal of Cleaner Production
JF - Journal of Cleaner Production
M1 - 144679
ER -