Experimental study on low temperature NO reduction and Hg0 removal of activated carbon loaded by Mn/Fe oxides
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摘要: 采用等体积浸渍法制备了Mn/Fe负载椰壳活性炭碳基催化剂Mn-Fe/HAC。在固定床实验台上研究了反应温度、体积空速(GHSV)和烟气组分(O2、CO、SO2和Hg0)对其脱硝脱汞性能的影响,并结合N2吸附-脱附、NH3-TPD、H2-TPR、Hg-TPD以及瞬态反应测试,分析其脱硝脱汞机理。结果表明,Mn/Fe负载可以明显促进碳基催化剂低温脱硝活性,添加Fe可提高催化剂表面的酸性位点数量和还原能力,促进催化剂活性,进一步拓宽其脱硝温度窗口;7Mn0.5Fe/HAC催化剂在160−220 ℃下的脱硝效率可达95%,且在100−220 ℃下Mn和Fe负载碳基催化剂脱汞效率基本稳定在100%。7Mn0.5Fe/HAC催化剂脱硝效率随着GHSV增加而逐渐降低,而脱汞效率则保持稳定。无O2条件下Mn/Fe催化剂脱硝效率较低(约为50%),而当烟气中O2含量大于6%,其脱硝效率可稳定在95%以上。Hg0浓度对Mn/Fe负载碳基催化剂脱硝性能影响不大,CO有一定抑制作用,而高浓度SO2抑制作用较为显著。Mn和Fe共负载可提高抗硫性,在含150 μL/L SO2模拟烟气下,7Mn0.5Fe/HAC催化剂在180 ℃的脱硝效率仍可稳定在80%以上。Mn/Fe负载碳基催化剂脱硝遵循E-R机理,即NH3先吸附于活性位点,再与气态NO反应,最终将NO还原为N2;而脱汞遵循L-H机理,即Hg0先吸附于活性位点,形成吸附态Hg0,然后与活性氧以及吸附态NO2与SO2反应分别生成HgO、Hg(NO3)2和HgSO4。Abstract: Mn-Fe/HAC carbon-based catalysts was prepared by equivalent-volume impregnation with coconut shell activated carbon as carrier and Mn(NO3)2 and Fe(NO3)3·9H2O as active components. NO reduction and Hg0 removal of carbon-based catalysts was carried out in a fixed-bed reactor. The effects of reaction temperature, gas hourly space velocity (GHSV) and flue gas components (O2, CO, Hg0 and SO2) on NO reduction and Hg0 removal were analyzed. The mechanisms of NO reduction and Hg0 removal over carbon-based catalysts were discussed based on the results of N2 adsorption-desorption, NH3-TPD, H2-TPR, Hg-TPD and transient response experiment. The obtained results indicate that NO reduction over carbon-based catalyst at low temperature can be enhanced significantly by Mn/Fe load, and Fe addition can increase the number of acid sites and the reducing capacity, which can improve NO reduction activity and further widen its temperature window on NO reduction. NO removal efficiency of 7Mn0.5Fe/HAC can reach 95% at 160−220 ℃, and Hg0 removal efficiency of carbon-based catalysts modified by Fe/Mn oxides is basically stable at 100% at 100−220 ℃. NO removal efficiency decreases and Hg0 removal efficiency is almost stable with increasing GHSV. A low NO removal efficiency of about 50% was obtained in absence of O2, however, high NO removal efficiency of more than 95% was present in the presence of more than 6% O2 in flue gas. Hg0 concentration has little effect on NO reduction of carbon-based catalyst modified by Mn/Fe, CO has a certain inhibitory effect, while high concentration SO2 has a significant inhibitory effect, and Mn/Fe co-loaded carbon-based catalyst improves tolerance to SO2. The NO removal efficiency of 7Mn0.5Fe/HAC can reach more than 80% at 180 ℃, 150 μL/L SO2. Carbon-based catalyst by loaded Mn/Fe for NO reduction follows E-R mechanism, i.e., NH3 first adsorbs on the active site, then reacts with gaseous NO, and finally reduces NO to N2. However, Hg0 removal follows L-H mechanism, i.e., Hg0 is first absorbed on the active site and forms absorbed Hg0, then reacts with reactive oxygen species and absorbed NO2 and SO2 to form HgO, Hg(NO3)2 and HgSO4, respectively.
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表 1 椰壳活性炭的理化特性参数
Table 1 Parameters of physiochemical property of CAC
Carrier BET surface area Ash Particle size Elemental analysis w/% /(m2·g−1) w/% mesh C H O N S CAC 515.1 15 5−8 71.79 2.02 25.78 0.32 0.09 表 2 模拟烟气组分
Table 2 Simulated flue gas composition
O2/% CO2/% NO/(μL·L−1) NH3/(μL·L−1) SO2/(μL·L−1) CO/(μL·L−1) Hg0/(μg·m−3) N2/% 6−16 12 400 400 ~150 ~8000 ~90 balance gas 表 3 碳基催化剂的比表面积及孔结构参数
Table 3 Specific surface area and pore structure parameters of carbon-based catalysts
Carbon-based catalyst BET surface area
/(m2·g−1)Total pore volume
/(cm3·g−1)Average pore diameter
/nmHAC 441.6 0.186 1.051 0.5Fe/HAC 511.9 0.237 0.483 1Fe/HAC 535.6 0.240 0.503 7Mn/HAC 502.6 0.233 1.051 7Mn0.5Fe/HAC 502.3 0.215 1.051 7Mn/HAC(S) 437.1 0.192 0.548 7Mn0.5Fe/HAC(S) 427.6 0.193 0.483 -
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