TY - JOUR
T1 - Carbonation of serpentinite rock from Lithuania and Finland
AU - Stasiulaitiene, Inga
AU - Fagerlund, Johan
AU - Nduagu, Experience
AU - Denafas, Gintaras
AU - Zevenhoven, Ron
N1 - Funding Information:
This work was partly funded by the Academy of Finland Research programme "Sustainable Energy" (2008-2011). The Geological Survey of Finland is acknowledged for producing the maps in Figure 2 as part of earlier project cooperation. Thomas Björklöf of ÅA is acknowledged for supporting the extraction data analysis and parameter modeling. Dr. Mai Uibu from Tallinn Technical University, Tallinn, is acknowledged for SSA analysis of Mg(OH)2 produced fromLithuanian serpentinite.
Copyright:
Copyright 2017 Elsevier B.V., All rights reserved.
PY - 2011
Y1 - 2011
N2 - CO2 mineral sequestration, or mineral carbonation, is presumably the most important CCS alternative when underground CO2 sequestration is not an option or considered unattractive. The following advantages must be emphasized: leakage-free CO2 fixation that does not require post-storage monitoring; the overwhelmingly large capacity offered by mineral resources available worldwide; and as recognized more recently, the possibility to operate with the CO2 containing gas directly, removing the very expensive CO2 separation step from the CCS process chain. Also, the solid products can be used in applications ranging from land reclamation to iron- and steelmaking. Here, a staged process for mineral sequestration that resulted from a decade of R&D work in Finland is applied to two serpentinite rocks from Lithuania and Finland, respectively. The process involves production of magnesium hydroxide from the mineral, with ammonium sulphate as the extractant (which is recovered downstream), followed by carbonation in a pressurized fluidized bed at 20-40 bar, 450-550°C. Benefits of this route are that 1) the carbonation reaction heat is taken benefit of, 2) only magnesium hydroxide is carbonated, 3) solid residue, magnesium carbonate and iron oxides are obtained as separate streams, 4) no expensive or non-recoverable chemical additives are used and 5) the pressure in the carbonation process is relatively low. The results show that magnesium hydroxide can be effectively extracted from the two serpentinites at somewhat different extraction process conditions, while the magnesium hydroxide particles produced (∼170μm, ∼340 μm) can be carbonated for 45-50 % within 10 minutes at 20 bar, ∼500°C. Process energy efficiency is similar, or slightly better than (direct, aqueous solution) carbonation processes that were suggested earlier.
AB - CO2 mineral sequestration, or mineral carbonation, is presumably the most important CCS alternative when underground CO2 sequestration is not an option or considered unattractive. The following advantages must be emphasized: leakage-free CO2 fixation that does not require post-storage monitoring; the overwhelmingly large capacity offered by mineral resources available worldwide; and as recognized more recently, the possibility to operate with the CO2 containing gas directly, removing the very expensive CO2 separation step from the CCS process chain. Also, the solid products can be used in applications ranging from land reclamation to iron- and steelmaking. Here, a staged process for mineral sequestration that resulted from a decade of R&D work in Finland is applied to two serpentinite rocks from Lithuania and Finland, respectively. The process involves production of magnesium hydroxide from the mineral, with ammonium sulphate as the extractant (which is recovered downstream), followed by carbonation in a pressurized fluidized bed at 20-40 bar, 450-550°C. Benefits of this route are that 1) the carbonation reaction heat is taken benefit of, 2) only magnesium hydroxide is carbonated, 3) solid residue, magnesium carbonate and iron oxides are obtained as separate streams, 4) no expensive or non-recoverable chemical additives are used and 5) the pressure in the carbonation process is relatively low. The results show that magnesium hydroxide can be effectively extracted from the two serpentinites at somewhat different extraction process conditions, while the magnesium hydroxide particles produced (∼170μm, ∼340 μm) can be carbonated for 45-50 % within 10 minutes at 20 bar, ∼500°C. Process energy efficiency is similar, or slightly better than (direct, aqueous solution) carbonation processes that were suggested earlier.
KW - Mineral carbonation
KW - Serpentinite
UR - http://www.scopus.com/inward/record.url?scp=79955393399&partnerID=8YFLogxK
U2 - 10.1016/j.egypro.2011.02.205
DO - 10.1016/j.egypro.2011.02.205
M3 - Article
AN - SCOPUS:79955393399
SN - 1876-6102
VL - 4
SP - 2963
EP - 2970
JO - Energy Procedia
JF - Energy Procedia
ER -