[1] Zhang Y., Zhu J., Lyu Q., et al., The ultra-low NOx emission characteristics of pulverized coal combustion after high temperature preheating. Fuel, 2020, 277: 118050.
[2] China’s National Economy and Social Development Statistical Bulletin in 2015, National Bureau of Statistics of China, 2015.
[3] Gui X., Liu J., Cao Y., et al., Coal preparation technology: Status and development in China. Energy & Environment, 2015, 26(6–7): 997–1013.
[4] Zheng J.H., Xu C.Y., Hu P.F., Study on flotation process of coal slime. Advanced Materials Research, 2013, 734–737: 1093–1096.
[5] Yang H., Guangxi Y., Junfu L., et al., An update of circulating fluidised bed combustion (CFB) technology in China. VGB PowerTech, 2012, 92(12): 75–79.
[6] Yue G., Cai R., Lu J., et al., From a CFB reactor to a CFB boiler – The review of R&D progress of CFB coal combustion technology in China. Powder Technology, 2016. DOI: 10.1016/j.powtec.2016.10.062
[7] Koornneef J., Junginger M., Faaij A., Development of fluidized bed combustion-An overview of trends, performance and cost. Progress in Energy & Combustion Science, 2007, 33(1): 19–55.
[8] Carlos Lupiáez., Guedea I., Bolea I., et al., Experimental study of SO2 and NOx emissions in fluidized bed oxy-fuel combustion. Fuel Processing Technology, 2013, 106: 587–594.
[9] Adams D., Oh D., Kim D., et al., Prediction of SOx-NOx emission from a coal-fired CFB power plant with machine learning: Plant data learned by deep neural network and least square support vector machine. Journal of Cleaner Production, 2020, 270: 122310.
[10] Miccio F., Gerhard Löffler., Wargadalam V.J., et al., The influence of SO2 level and operating conditions on NOx and N2O emissions during fluidised bed combustion of coals. Fuel, 2001, 80(11): 1555–1566.
[11] Spliethoff H., Basic effect on NOx emission in air staging and reburning at a bench-scale test facility. Fuel, 1996, 75(5): 560–564.
[12] Lyngfelt A., Åmand L.E., Leckner B., Reversed air staging-a method for reduction of N2O emissions from fluidized bed combustion of coal. Fuel, 1998, 77(9): 953–959.
[13] Smart J.P., Morgan D.J., The effectiveness of multi-fuel reburning in an internally fuel-staged burner for NOx reduction. Fuel, 1994, 73(9): 1437–1442.
[14] Mereb J.B., Wendt J.O.L., Air staging and reburning mechanisms for NOx abatement in a laboratory coal combustor. Fuel, 1994, 73(7): 1020–1026.
[15] Emis, https://emis.vito.be/en/techniekfiche/selective-catalytic-reduction, 2018.
[16] Emis, https://emis.vito.be/en/techniekfiche/selective-non-catalytic-reduction, 2018.
[17] Mok Y.S., Lee H.J., Removal of sulfur dioxide and nitrogen oxides by using ozone injection and absorption-reduction technique. Fuel Processing Technology, 2006, 87(7): 591–597.
[18] Arthur L. Kohl., Richard B., Nielsen., gas purification, fifth Ed., Gulf Professional Publishing, 1997, pp. 466–669.
[19] IEA (2006). Flue gas desulfurization (FGD) for SO2 control. http://www.iea-coal.org.uk/.
[20] Warych J., Szymanowski M., Optimum values of process parameters of the wet limestone flue gas desulfurization system. Chemical Engineering & Technology, 2015, 25(4): 427–432.
[21] Ma S., Chai J., Jiao K., et al., Environmental influence and countermeasures for high humidity flue gas discharging from power plants. Renewable and Sustainable Energy Reviews, 2017, 73: 225–235.
[22] Zhang L., Dong X., Hou F., et al., Study on optimization experiment of SCR denitrification technologies in a coal-fired power plant. IOP Conference Series: Earth and Environmental Science, Weihai, China, 2018.
DOI: 10.1088/1755-1315/108/5/052100.
[23] Yang W., Summary of flue gas denitration technology for coal-fired power plants. IOP Conference Series: Earth and Environmental Science, Wuhan, China, 2019, 300: 032054. DOI: 10.1088/1755-1315/300/3/032054.
[24] Hu Z., Jiang E., Ma X., Numerical simulation on operating parameters of SNCR process in a municipal solid waste incinerator. Fuel, 2019, 245: 160–173.
[25] Zhou T., Gong Z., Lu Q., et al., Experimental study on enhanced control of NOx emission from circulating fluidized bed combustion. Energy & Fuels, 2015, 29(6): 3634–3639.
[26] Gong Z., Zhou T., Lu Q., et al., Combustion and NOx emission characteristics of Shenmu char in a circulating fluidized bed with post-combustion. Energy & Fuels, 2016, 30(1): 31–38.
[27] Zhou T., Lu Q., Cao Y., et al., Study on the combustion and NOx emission characteristics of low rank coal in a circulating fluidized bed with post-combustion. The Canadian Journal of Chemical Engineering, 2017, 95(12): 2333–2340.
[28] Xiao Y., Song G.L., Song W.J., et al., Influence of feeding position and post-combustion air arrangement on NOx emission from circulating fluidized bed combustion with post-combustion. Fuel, 2020, 269: 117394.
[29] Lyngfelt A., Bergqvist K., Johnsson F., et al., Dependence of sulphur capture performance on air staging in a 12 MW circulating fluidized bed boiler. Springer Netherlands, 1993.
[30] Saastamoinen J.J., Particle-size optimization for SO2 capture by limestone in a circulating fluidized bed. Industrial & Engineering Chemistry Research, 2007, 46(22): 7308–7316.
[31] Montagnaro F., Salatino P., Scala F., The influence of temperature on limestone sulfation and attrition under fluidized bed combustion conditions. Experimental Thermal & Fluid Science, 2010, 34(3): 352–358.
[32] Anders L., Bo L., Sulphur capture in fluidized bed boilers: The effect of reductive decomposition of CaSO4. The Chemical Engineering Journal, 1989, 40: 59–69.
[33] Jensen A., Johnsson J.E., Dam-Johansen K., Nitrogen chemistry in FBC with limestone addition. Symposium on Combustion, 1997, 26(2): 3335–3342.
[34] Diego L.F.D., Londono C.A., Wang X.S., et al., Influence of operating parameters on NOx and N2O axial profiles in a circulating fluidized bed combustor. Fuel, 1996, 75(8): 971–978.
[35] Wang H., Guo S., Liu D., et al., Influence of water vapor on surface morphology and pore structure during limestone calcination in a laboratory-scale fluidized bed. Energy & Fuels, 2016, 30(5): 3821–3830.
[36] Jensen A., Johnsson J.E., Dam-Johansen K., Nitrogen chemistry in FBC with limestone addition. Symposium on Combustion, 1997, 26(2): 3335–3342.
[37] Derek G. Gavin., Mark A. Dorrington., Factors in the conversion of fuel nitrogen to nitric and nitrous oxides during fluidized bed combustion. Fuel, 1993, 72: 381–388.
[38] Tadaaki S., Yutaka T., Ayumu K., et al., Effect of SO2 removal by limestone on NOx and N2O emissions from a bubbling fluidized-bed combustor. Fuel, 1992, 71: 841–844.
[39] Johnsson J.E., Formation and reduction of nitrogen oxides in fluidized-bed combustion. Fuel, 1994, 73(9): 1398–1415.
[40] Dam-Johansen K., Amand L.E., Leckner B., Influence of SO2 on the NO/N2O chemistry in fluidized bed combustion: 2. Interpretation of full-scale observations based on laboratory experiments. Fuel, 1993, 72(4): 565–571.