TY - JOUR
T1 - Carbonation of magnesium silicate mineral using a pressurised gas/solid process
AU - Fagerlund, Johan
AU - Teir, Sebastian
AU - Nduagu, Experience
AU - Zevenhoven, Ron
N1 - Funding Information:
This work was funded by Nordic Energy Research (2003-2007), the Academy of Finland Research programme "Sustainable Energy" (2008-2011) and KH Renlund Foundation (2007, 2008).
Copyright:
Copyright 2011 Elsevier B.V., All rights reserved.
PY - 2009/2
Y1 - 2009/2
N2 - Carbon dioxide mineral sequestration is not as widely advocated as CO2 sequestration by other means such as underground storage alternatives, yet it possesses properties (capacity, permanency, energy economy) that can not be matched by other options. In this paper, our findings and results since GHGT-8 as well as current activities and near-future plans regarding CO2 mineral carbonation are presented. The focus lies on the use of fluidised bed (FB) reactors for the carbonation of magnesium silicates via magnesium oxide or magnesium hydroxide intermediates, at temperatures and pressures up to 600 {ring operator}C, 100 bar (allowing for both sub- and supercritical conditions for CO2), supported by earlier experiments using pressurised thermogravimetric analysis (PTGA). In addition, as the production of reactive magnesium from silicate mineral is not straightforward, it receives special attention, and first results of magnesium hydroxide production from serpentine using different methods are presented.
AB - Carbon dioxide mineral sequestration is not as widely advocated as CO2 sequestration by other means such as underground storage alternatives, yet it possesses properties (capacity, permanency, energy economy) that can not be matched by other options. In this paper, our findings and results since GHGT-8 as well as current activities and near-future plans regarding CO2 mineral carbonation are presented. The focus lies on the use of fluidised bed (FB) reactors for the carbonation of magnesium silicates via magnesium oxide or magnesium hydroxide intermediates, at temperatures and pressures up to 600 {ring operator}C, 100 bar (allowing for both sub- and supercritical conditions for CO2), supported by earlier experiments using pressurised thermogravimetric analysis (PTGA). In addition, as the production of reactive magnesium from silicate mineral is not straightforward, it receives special attention, and first results of magnesium hydroxide production from serpentine using different methods are presented.
KW - Carbon dioxide storage
KW - gas/solid carbonation
KW - Mg(OH)
KW - Mineral carbonation
KW - Serpentinite
UR - http://www.scopus.com/inward/record.url?scp=67650104707&partnerID=8YFLogxK
U2 - 10.1016/j.egypro.2009.02.321
DO - 10.1016/j.egypro.2009.02.321
M3 - Conference article
AN - SCOPUS:67650104707
SN - 1876-6102
VL - 1
SP - 4907
EP - 4914
JO - Energy Procedia
JF - Energy Procedia
IS - 1
T2 - 9th International Conference on Greenhouse Gas Control Technologies, GHGT-9
Y2 - 16 November 2008 through 20 November 2008
ER -