[1] C.M. Nam, B.M. Gibbs, Application of the thermal deNOx process to dieselengine deNOx: an experimental and kinetic modeling study, Fuel 81 (2002)1359-1367.[2] K.H. Han, C.M. Lu, Y.Z.Wang, N.S. Niu, Z.C. Liu,W.D. Hao, Experimental study on de-NOx characteristics of selective non-catalytic reduction, Proc. Chin. Soc. Electron. Eng.28 (14) (2008) 80-85 (in Chinese).[3] R. Rota, D. Antos, E.F. Zanoelo, M.Morbidelli, Experimental and modeling analysis ofthe NOxOUT process, Chem. Eng. Sci. 57 (2002) 27-38.[4] M.T. Javed, N. Irfan, B.M. Gibbs, Control of combustion-generated nitrogen oxides byselective non-catalytic reduction, J. Environ. Manag. 83 (2007) 251-289.[5] D.L. Siebers, J.A. Caton, Removal of nitric oxide from exhaust gas with cyanuric acid,Combust. Flame 79 (1990) 31-46.[6] P. Glarborg, P.G. Kristensen, S.H. Jensen, K.D. Johansen, A flow reactor study of HNCOoxidation chemistry, Combust. Flame 98 (1994) 241-258.[7] G.W. Lee, B.H. Shon, J.G. Yoo, J.H. Jung, K.J. Oh, The influence of mixing between NH3 and NO for a de-NOx reaction in the SNCR process, J. Ind. Eng. Chem. 14 (2008)457-467.[8] W.H.J. Graus, E. Worrel, Effect of SO2 and NOx control on energy-efficiency powergeneration, Energ Policy 35 (7) (2007) 3898-3908.[9] W.J. Yang, Z.J. Zhou, J.H. Zhou, H.K. Lv, J.Z. Liu, K.F. Cen, Application of hybrid coalreburning/SNCR processes for NOx reduction in a coal-fired boiler, Environ. Eng.Sci. 26 (2) (2009) 311-317.[10] H.Y. Kim, S.W. Baek, C.Y. Lee, Effects of hybrid reburning system with SNCR and airstaging on NOx reduction and thermal characteristics in oxygen enhanced combustion,Combust. Sci. Technol. 181 (10) (2009) 1289-1309.[11] W.J. Yang, Z.C. Chen, Z.J. Zhou, Z.H. Wang, J.H. Zhou, Z.Y. Huang, K.F. Cen, Costefficientnitrogen oxides control by a hybrid selective noncatalytic reduction and selectivecatalytic reduction system on a utility boiler, Environ. Eng. Sci. 28 (5) (2011)341-348.[12] K. Myöhänen, T. Hyppänen, T. Pikkarainen, T. Eriksson, A. Hotta, Near zero CO2 emissionsin coal firing with oxy-fuel circulating fluidized bed boiler, Chem. Eng. Technol.32 (3) (2009) 355-363.[13] Q.Z. Li, C.S. Zhao, W.F. Wu, X.P. Chen, W. Dong, Experimental investigation on NOemission characteristic during pulverized coal combustion in O2/CO2 environment,Proc. Chin. Soc. Electron. Eng. 29 (23) (2009) 33-39 (in Chinese).[14] L.B. Duan, C.S. Zhao, J.Y. Lu,W. Zhou, Y.J. Li, X.P. Chen, SO2/NO emission characteristicsduring O2/CO2 coal combustion process, J. Chem. Ind. Eng. Soc. China 60 (5)(2009) 1270-1274 (in Chinese).[15] H. Liu, R. Zailani, B. Gibbs, Comparisons of pulverized coal combustion in air and inmixtures of O2/CO2, Fuel 84 (2005) 833-840.[16] R. Zhao, H. Liu, H. Hu, X.J. Zhong, Z.J. Wang, Z.Y. Xu, J.R. Qiu, Experimental andmodeling study of NO emission under high CO2 concentration, Sci. Chin. Technol.Sci. 53 (12) (2010) 3275-3283.[17] Z.M. Lu, J.D. Lu, Influence of O2 concentration on NO reduction and N2O formation inthermal deNOx process, Combust. Flame 156 (2009) 1303-1315.[18] B.C. Moo, F.C. Chin, Low temperature SNCR process for NOx control, Sci. Total Environ.198 (1997) 73-78.[19] J.A. Miller, P. Glarborg, Modeling the formation of N2O and NO2 in the thermal de-NOx process, in: M. Bodenstein, J. Wolfrum, H.R. Volppp, R. Rannacher, J. Warnatz(Eds.), Gas Phase Chemical Reaction Systems: Experiments and Models 100 YearsAfter, Springer Series in Chemical Physics, 1996, pp. 318-333.[20] M.J. Pill, T. Turanyi, K.J. Hughes, “Irreversible mechanism mole Kelvin units”, TheUniversity of Leeds, http://garfield.chen.elte.hu/Combustion/mechanisms 2004.[21] R. Rota, E.F. Zanoelo, Influence of oxygenated additives on the NOxOUT process efficiency,Fuel 82 (2003) 765-770.[22] V.M. Zamansky, V.V. Lissianski, P.M. Maly, L. Ho, D. Rusli,W.C. Gardiner, Reaction ofsodium species in the promoted SNCR process, Combust. Flame 117 (1999) 821-831.[23] M.D. Rumminger, D. Reinelt, V. Babushok, G.T. Linteris, Numerical study of the inhibitionof premixed and diffusion flames by iron pentacarbonyl, Combust. Flame 116(1999) 207-219.[24] A.E. Lutz, R.J. Kee, J.A. Miller, SENKIN: a FORTRAN program for predicting homogeneousgas phase chemical kinetics with sensitivity analysis, Sandia National LaboratoriesReport, SAND87-8248, 1988.[25] D.M. Hamby, A review of techniques for parameter sensitivity analysis of environmentalmodels, Environ. Monit. Assess. 32 (2) (1994) 135-154.[26] T. Turányi, Sensitivity analysis of complex kinetic systems. Tools and applications, J.Math. Chem. 5 (3) (1990) 203-248.[27] S.H. Wu, Q.X. Cao, H. Liu, Q. An, X. Huang, Experimental and modeling study of theeffects of gas additives on the thermal deNOx process, Chin. J. Chem. Eng. 18 (1)(2010) 143-148.[28] L. Gasnot, D.Q. Dao, J.F. Pauwels, Experimental and kinetic study of the effect of additiveson the ammonia based SNCR process in low temperature conditions, EnergyFuel 26 (5) (2012) 2837-2849.[29] S.L. Niu, K.H. Han, C.M. Lu, Experimental study on the effect of urea and additive injectionfor controlling nitrogen oxides emissions, Environ. Eng. Sci. 27 (1) (2010)47-53.[30] J.A. Silver, The effect of sulfur on the thermal deNOx process, Combust. Flame 53(1-3) (1983) 17-21.[31] W.J. Yang, J.H. Zhou, J.J. Zhou, Z.C. Chen, J.Z. Liu, K.F. Cen, Action of oxygen and sodiumcarbonate in the urea-SNCR process, Combust. Flame 156 (2009) 1785-1790.[32] K.H. Han, C.M. Lu, Kinetic model and simulation of promoted selective non-catalyticreduction by sodium carbonate, Chin. J. Chem. Eng. 15 (4) (2009) 512-519.[33] S.L. Niu, K.H. Han, C.M. Lu, An experimental study on the effect of operating parametersand sodium additive on the NOxOUT process, Process Saf. Environ. 89 (2011) 121-126.[34] M.T. Javed, W. Nimmo, A. Mahmood, N. Irfan, Effect of oxygenated liquid additiveson the urea based SNCR process, J. Environ. Manag. 90 (2009) 3429-3435. |