参考文献/References:
[1] Lyngfelt A,Leckner B.Combustion of wood-chips in circulating fluidized bed boilers-NO and CO emissions as functions of temperature and air-staging [J]. Fuel,1999,78(9):1065-1072.
[2] Roesler J F,Yetter R A,Dryer F L.Kinetic interaction of CO,NOx and HCl emissions in postcombustion gases [J].Combustion and Flame, 1995,100(3):495-504.
[3] Andries J,Verloop M,Hein K.Co-combustion of coal and biomass in a pressurized bubbling fluidized bed [A].In:Proceedings of the 14th International Conference on FBC [C].Vancouver,Canada,1997.313-320.
[4] Armesto L,Cabanillas A,Bahillo A.Coal and biomass co-combustion on fluidized bed:comparison of circulating and bubbling fluidized bed technologies [A].In:Proceedings of the 14th International Conference on FBC [C].Vancouver,Canada,1997.301-312.
[5] Desroches-Ducarne Estelle,Eric Marty,Dolignier J christophe,et al.Modeling of gaseous pollutants emissions in circulating fluidized bed combustion of municipal refuse [J]. Fuel, 1998,77(12):1311-1315.
[6] Arsen J Darnary.Statistical record of the environment [M].second edition.Detroit:Gale Research Inc,1994.455-489.
[7] 刘柏谦.吉林市城市生活垃圾特性研究[J].东北电力学院报,1999,19(3):16-22.
Liu Baiqian.Municipal solid waste characteristics of Jilin city [J].Journal of Northeast China Institute of Electric Power Engineering, 1999,19(3):16-22.(in Chinese)
[8] Matsuka M,Takeda K,Miyatani T.Simultaneous chlorination and sulphation of calcined limestone [J].Chemical Engineering Science,1996, 51(11):2529-2534.
[9] Nordin Anders.Optimization of sulfur retention in ash when co-combusting high sulfur fuels and biomass fuels in a small pilot scale fluidized bed [J].Fuel,1995, 74(4):615-622.
[10] Lisa K,Salokoski P,Hupa A.Heterogeneous formation and destruction of nitrous oxide under fluidized bed combustion conditions [A].In: Proceeding 11th International Conference on Fluidized Bed Combustion [C].New York:ASME,1991.1027-1033.
[11] Kilpinen P,Hupa M.Homogeneous N2O chemistry at fluidized bed combustion conditions:a kinetic modeling study [J].Combustion and Flame,1991,85(1):94-104.
相似文献/References:
[1]房德山,冷伟,徐治皋,等.循环流化床锅炉传热特性分析[J].东南大学学报(自然科学版),2001,31(6):52.[doi:10.3969/j.issn.1001-0505.2001.06.012]
Fang Deshan,Leng Wei,Xu Zhigao,et al.Analysis of Heat Transfer Characteristics in Circulating Fluidized Bed Boiler[J].Journal of Southeast University (Natural Science Edition),2001,31(1):52.[doi:10.3969/j.issn.1001-0505.2001.06.012]
[2]陶敏,金保升,仲兆平,等.循环流化床烟气脱硫多层喷水数学模型[J].东南大学学报(自然科学版),2010,40(1):144.[doi:10.3969/j.issn.1001-0505.2010.01.027]
Tao Min,Jin Baosheng,Zhong Zhaoping,et al.Mathematical model for multi-level humidifying of the circulating fluidized bed-flue gas desulfurization system[J].Journal of Southeast University (Natural Science Edition),2010,40(1):144.[doi:10.3969/j.issn.1001-0505.2010.01.027]
[3]刘仁平,金保升,仲兆平,等.循环流化床燃烧棉秆两种床料的特性[J].东南大学学报(自然科学版),2007,37(3):441.[doi:10.3969/j.issn.1001-0505.2007.03.018]
Liu Renping,Jin Baosheng,Zhong Zhaoping,et al.Study on two kinds of bed materials during CFB combustion of cotton stalk[J].Journal of Southeast University (Natural Science Edition),2007,37(1):441.[doi:10.3969/j.issn.1001-0505.2007.03.018]
[4]向文国,徐祥,肖云汉.循环流化床上升段流体动力特性数值模拟[J].东南大学学报(自然科学版),2005,35(5):752.[doi:10.3969/j.issn.1001-0505.2005.05.021]
Xiang Wenguo,Xu Xiang,Xiao Yunhan.Fluid dynamics numerical simulation for riser of circulating fluidized bed[J].Journal of Southeast University (Natural Science Edition),2005,35(1):752.[doi:10.3969/j.issn.1001-0505.2005.05.021]
[5]周建新,邵壮,李崇,等.基于Aspen平台的Oxy-CFB燃烧侧动态特性模拟[J].东南大学学报(自然科学版),2014,44(6):1187.[doi:10.3969/j.issn.1001-0505.2014.06.017]
Zhou Jianxin,Shao Zhuang,Li Chong,et al.Dynamic characteristics of Oxy-CFB combustion system based on Aspen[J].Journal of Southeast University (Natural Science Edition),2014,44(1):1187.[doi:10.3969/j.issn.1001-0505.2014.06.017]