Reactivity of alkaline lignite fly ashes towards CO2 in water

被引:86
作者
Back, Martin [1 ]
Kuehn, Michael
Stanjek, Helge
Peiffer, Stefan
机构
[1] Univ Bayreuth, BayCEER, Dept Hydrol, D-95440 Bayreuth, Germany
关键词
D O I
10.1021/es702760v
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The reaction kinetics between alkaline lignite fly ashes and CO2 (pCO(2) = 0.01 -0.03 MPa) were studied in a laboratory CO2 flow through reactor at 25-75 degrees C. The reaction is characterized by three phases that can be separated according to the predominating buffering systems and the rates Of CO2 uptake. Phase I (pH > 12, < 30 min) is characterized by the dissolution of lime, the onset of calcite precipitation and a maximum uptake, the rate of which seems to be limited by dissolution Of CO2 Phase II (pH < 10.5,10-60 min) is dominated by the carbonation reaction. CO2 uptake in phase III (pH < 8.3) is controlled by the dissolution of periclase (MgO) leading to the formation of dissolved magnesium-bicarbonate. Phase I could be significantly extended by increasing the solid-liquid ratios and temperature, respectively. At 75 degrees C the rate of calcite precipitation was doubled leading to the neutralization of approximately 0.23 kg CO2 per kg fly ash within 4.5 h, which corresponds to nearly 90% of the total acid neutralizing capacity.
引用
收藏
页码:4520 / 4526
页数:7
相关论文
共 21 条
[1]  
BERGMANN J, 1998, EPDIC 5 1, V278, DOI UNSP 300305
[2]   Investigation of accelerated carbonation for the stabilisation of MSW incinerator ashes and the sequestration of CO2 [J].
Bertos, MF ;
Li, X ;
Simons, SJR ;
Hills, CD ;
Carey, PJ .
GREEN CHEMISTRY, 2004, 6 (08) :428-436
[3]   THE KINETICS OF CALCITE DISSOLUTION AND PRECIPITATION IN GEOLOGICALLY RELEVANT SITUATIONS OF KARST AREAS .1. OPEN SYSTEM [J].
BUHMANN, D ;
DREYBRODT, W .
CHEMICAL GEOLOGY, 1985, 48 (1-4) :189-211
[4]  
*COMM DEC, 2000, OFFICIAL J EUROPEAN, pL226
[5]  
*DIW, 2005, INNOVATIVE ENERGY TE
[6]   A review of accelerated carbonation technology in the treatment of cement-based materials and sequestration of CO2 [J].
Fernández Bertos, M ;
Simons, SJR ;
Hills, CD ;
Carey, PJ .
JOURNAL OF HAZARDOUS MATERIALS, 2004, 112 (03) :193-205
[7]   Precipitation in the Mg-carbonate system -: effects of temperature and CO2 pressure [J].
Haenchen, Markus ;
Prigiobbe, Valentina ;
Baciocchi, Renato ;
Mazzotti, Marco .
CHEMICAL ENGINEERING SCIENCE, 2008, 63 (04) :1012-1028
[8]   Mineral CO2 sequestration by steel slag carbonation [J].
Huijgen, WJJ ;
Witkamp, GJ ;
Comans, RNJ .
ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2005, 39 (24) :9676-9682
[9]   Mechanisms of aqueous wollastonite carbonation as a possible CO2 sequestration process [J].
Huijgen, Wouter J. J. ;
Witkamp, Geert-Jan ;
Comans, Rob N. J. .
CHEMICAL ENGINEERING SCIENCE, 2006, 61 (13) :4242-4251
[10]   Energy consumption and net CO2 sequestration of aqueous mineral carbonation [J].
Huijgen, Wouter J. J. ;
Ruijg, Gerrit Jan ;
Comans, Rob N. J. ;
Witkamp, Geert-Jan .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2006, 45 (26) :9184-9194