The impact of wet flue gas desulfurization scrubbing on mercury emissions from coal-fired power stations

被引:32
作者
Niksa, S [1 ]
Fujiwara, N
机构
[1] Niksa Energy Associates, Belmont, CA 94002 USA
[2] Idemitsu Kosan Co Ltd, Coal Res Lab, Chiba, Japan
关键词
D O I
10.1080/10473289.2005.10464689
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
This article introduces a predictive capability for Hg retention in any Ca-based wet flue gas desulfurization (FGD) scrubber, given mercury (Hg) speciation at the FGD inlet, the flue gas composition, and the sulphur dioxide (SO,) capture efficiency. A preliminary statistical analysis of data from 17 full-scale wet FGDs connects flue gas compositions, the extents of Hg oxidation at FGD inlets, and Hg retention efficiencies. These connections clearly signal that solution chemistry within the FGD determines Hg retention. A more thorough analysis based on thermochemical equilibrium yields highly accurate predictions for total Hg retention with no parameter adjustments. For the most reliable data, the predictions were within measurement uncertainties for both limestone and Mg/lime systems operating in both forced and natural oxidation mode. With the U.S. Environmental Protection Agency's (EPA) Information Collection Request (ICR) database, the quantitative performance was almost as good for the most modern FGDs, which probably conform to the very high SO, absorption efficiencies assumed in the calculations. The large discrepancies for older FGDs are tentatively attributed to the unspecified SO2 capture efficiencies and operating temperatures and to the possible elimination of HCl in prescrubbers. The equilibrium calculations suggest that Hg retention is most sensitive to inlet HCl and O-2 levels and the FGD temperature; weakly dependent on SO2 capture efficiency; and insensitive to HgCl2, NO, CA:S ratio, slurry dilution level in limestone FGDs, and MgSO3 levels in Mg/lime systems. Consequently, systems with prescrubbers to eliminate HCl probably retain less Hg than fully integrated FGDs. The analysis also predicts re-emission of Hg-o but only for inlet O-2 levels that are much lower than those in full-scale FGDs.
引用
收藏
页码:970 / 977
页数:8
相关论文
共 12 条
[1]  
AFONSO R, 2001, P US EPADOEEPRI COMB
[2]  
CHANG J, 2003, P US EPADOEEPRI COMB
[3]  
CHU P, 2001, P US EPADOEEPRI COMB
[4]   Flue gas Hg measurements from coal-fired boilers equipped with wet scrubbers [J].
DeVito, MS ;
Withum, JA ;
Statnick, RM .
INTERNATIONAL JOURNAL OF ENVIRONMENT AND POLLUTION, 2002, 17 (1-2) :126-142
[5]  
EVANS AP, 1998, DEFC2294PC94251
[6]   Experimental investigation and modeling of a wet flue gas desulfurization pilot plant [J].
Kiil, S ;
Michelsen, ML ;
Dam-Johansen, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (07) :2792-2806
[7]   A study of the thermodynamic behavior of mercury in a wet flue gas cleaning process [J].
Krissmann, J ;
Siddiqi, MA ;
Peters-Gerth, P ;
Ripke, M ;
Lucas, K .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1998, 37 (08) :3288-3294
[8]   The CRH1 receptor antagonist R121919 attenuates stress-elicited sleep disturbances in rats, particularly in those with high innate anxiety [J].
Lancel, M ;
Müller-Preuss, P ;
Wigger, A ;
Landgraf, R ;
Holsboer, F .
JOURNAL OF PSYCHIATRIC RESEARCH, 2002, 36 (04) :197-208
[9]  
LAUDAL DL, 2001, DEFC2698FT40321 US D
[10]   COMPUTATION OF PHASE AND CHEMICAL-EQUILIBRIA IN FLUE-GAS WATER-SYSTEMS [J].
LUCKAS, M ;
LUCAS, K ;
ROTH, H .
AICHE JOURNAL, 1994, 40 (11) :1892-1900