TY - JOUR
T1 - CO2 sequestration by carbonation of steelmaking slags in an autoclave reactor
AU - Chang, E. E.
AU - Pan, Shu Yuan
AU - Chen, Yi Hung
AU - Chu, Hsiao Wen
AU - Wang, Chu Fang
AU - Chiang, Pen Chi
PY - 2011/11/15
Y1 - 2011/11/15
N2 - Carbon dioxide (CO2) sequestration experiments using the accelerated carbonation of three types of steelmaking slags, i.e., ultra-fine (UF) slag, fly-ash (FA) slag, and blended hydraulic slag cement (BHC), were performed in an autoclave reactor. The effects of reaction time, liquid-to-solid ratio (L/S), temperature, CO2 pressure, and initial pH on CO2 sequestration were evaluated. Two different CO2 pressures were chosen: the normal condition (700psig) and the supercritical condition (1300psig). The carbonation conversion was determined quantitatively by using thermo-gravimetric analysis (TGA). The major factors that affected the conversion were reaction time (5min to 12h) and temperature (40-160°C). The BHC was found to have the highest carbonation conversion of approximately 68%, corresponding to a capacity of 0.283kgCO2/kgBHC, in 12h at 700psig and 160°C. In addition, the carbonation products were confirmed to be mainly in CaCO3, which was determined by using scanning electron microscopy (SEM) and X-ray powder diffraction (XRD) to analyze samples before and after carbonation. Furthermore, reaction kinetics were expressed with a surface coverage model, and the carbon footprint of the developed technology in this investigation was calculated by a life cycle assessment (LCA).
AB - Carbon dioxide (CO2) sequestration experiments using the accelerated carbonation of three types of steelmaking slags, i.e., ultra-fine (UF) slag, fly-ash (FA) slag, and blended hydraulic slag cement (BHC), were performed in an autoclave reactor. The effects of reaction time, liquid-to-solid ratio (L/S), temperature, CO2 pressure, and initial pH on CO2 sequestration were evaluated. Two different CO2 pressures were chosen: the normal condition (700psig) and the supercritical condition (1300psig). The carbonation conversion was determined quantitatively by using thermo-gravimetric analysis (TGA). The major factors that affected the conversion were reaction time (5min to 12h) and temperature (40-160°C). The BHC was found to have the highest carbonation conversion of approximately 68%, corresponding to a capacity of 0.283kgCO2/kgBHC, in 12h at 700psig and 160°C. In addition, the carbonation products were confirmed to be mainly in CaCO3, which was determined by using scanning electron microscopy (SEM) and X-ray powder diffraction (XRD) to analyze samples before and after carbonation. Furthermore, reaction kinetics were expressed with a surface coverage model, and the carbon footprint of the developed technology in this investigation was calculated by a life cycle assessment (LCA).
KW - Accelerated carbonation
KW - Alkaline solid waste
KW - Calcite
KW - Life cycle assessment
KW - Surface coverage model
UR - http://www.scopus.com/inward/record.url?scp=80054114972&partnerID=8YFLogxK
UR - http://www.scopus.com/inward/citedby.url?scp=80054114972&partnerID=8YFLogxK
U2 - 10.1016/j.jhazmat.2011.08.006
DO - 10.1016/j.jhazmat.2011.08.006
M3 - Article
C2 - 21889848
AN - SCOPUS:80054114972
SN - 0304-3894
VL - 195
SP - 107
EP - 114
JO - Journal of Hazardous Materials
JF - Journal of Hazardous Materials
ER -