[1] DUAN L, DUAN Y, ZHAO C, et al.NO emission during co-firing coal and biomass in an oxy-fuel circulating fluidized bed combustor[J].Fuel,2015,150:8-13 10.1016/j.fuel.2015.01.110
[2] KLIMANEK A, ADAMCZYK W, KATELBACH-WOZNIAK A, et al.Towards a hybrid Eulerian-Lagrangian CFD modeling of coal gasification in a circulating fluidized bed reactor[J].Fuel,2015,152:131-137 10.1016/j.fuel.2014.10.058
[3] 宋健斐, 彭园园, 郭本玲, 等. 循环流化床烟气脱硫塔入口结构改进的数值模拟[J]. 环境工程学报,2010,4(10):2283-2286
[4] CHEN Y C, HWANG S J.Attrition and sulfation of calcium sorbent and solids circulation rate in an internally circulating fluidized bed[J].Powder Technology,2002,127(3):185-195
[5] JIANG M X, KEENER T C, KHANG S J.The use of a circulating fluidized bed absorber for the control of sulfur dioxide emissions by calcium oxide sorbent via in situ hydration[J].Powder Technology,1995,85(2):115-126 10.1016/0032-5910(95)03003-R
[6] 杨柳春, 杨文奇, 童志权. 内循环流化床烟气脱硫技术的实验研究[J]. 环境污染治理技术与设备,2005,6(2):62-65 10.3969/j.issn.1673-9108.2005.02.016
[7] 张浩, 程世庆, 胡云鹏,等. 流化床反应器石灰石固硫特性研究[J]. 环境工程学报,2011,5(2):395-398
[8] 范丽婷, 王福利, 李鸿儒. 循环流化床烟气脱硫系统内压降的建模[J]. 环境工程学报,2013,7(1):289-293
[9] 邱宽嵘, 张洪, 蒋玢. 氧化钙颗粒脱硫反应及数学模型的研究[J]. 燃料化学学报,1997,25(1):65-71
[10] 刘向军, 徐旭常. 生石灰粉和飞灰物料团脱硫反应的模型研究[J]. 工程热物理学报,2004,25(1):167-170 10.3321/j.issn:0253-231X.2004.01.050
[11] 马亮, 何榕, 曹立勇. 孔隙结构对燃煤脱硫反应最大转化率的影响[J]. 燃烧科学与技术,2013,19(5):395-399 10.11715/rskxjs.R201212022
[12] 邱宽嵘, 蒋玢.CaO颗粒脱硫化学反应研究[J]. 中国矿业大学学报,1996,25(4):93-97