超临界及超超临界循环流化床锅炉技术研究与应用

参考文献

[1]KoornneefJ,JungingerM,FaaijA.Development of fluidized bed combustion—an overview of trends,performance and cost[J].Progress in energy and combustion science,2007,33(1):19-55.

[2]吕俊复,于龙,岳光溪,等.循环流化床锅炉水冷壁的热流密度分布[J].动力工程,2007,27(3):336-340.LüJunfu,YuLong,YueGuangxi,et al.Heat flux distribution along water walls of circulating fluidized boilers[J].Journal of Power Engineering,2007,27(3):336-340(in Chinese).

[3]YerushalmiJ,Turner DH,Squires AM.The fast fluidized bed[J].Industrial & Engineering Chemistry Process Design and Development,1976,15(1):47-53.

[4]吴玉新,吕俊复,张建胜,等.800MWe超临界循环流化床锅炉概念设计[J].锅炉技术,2004,35(3):1-5,48.WuYuxin,LüJunfu,ZhangJiansheng,et al.Conceptual design of an 800MWe supercritical pressure circulating fluidized bed boiler[J].Boiler Technology,2004,35(3):1-5,48(in Chinese).

[5]LotharR,MartinH,Ludolf P.Methodofandapparatus for carrying out an exothermic process:U.S. Patent 4111158[P].1978-09-05.

[6]杨石,杨海瑞,吕俊复,等.新一代节能型循环流化床锅炉燃烧技术[J].动力工程,2009,29(8):728-732,788.YangShi,YangHairui,LüJunfu,et al.The new generation combustion technology for energy saving circulating fluidized bed boilers[J].Journal of Power Engineering,2009,29(8):728-732,788(in Chinese).

[7]Yang HR,ZhangH,Lu JF,et al.Novel CFB boiler technology with reconstruction of its fluidization state[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:195-199.

[8]岳光溪,吕俊复,徐鹏,等.循环流化床燃烧发展现状及前景分析[J].中国电力,2016,49(1):1-13.YueGuangxi,LüJunfu,XuPeng,et al.The up-to-date development and future of circulating fluidized bed combustion technology[J].Electric Power,2016,49(1):1-13(in Chinese).

[9]YueGuangxi,LuJunfu,ZhangHairui,et al.Design theory of circulating fluidized bed boilers[C]//Proceedings of the 18th International Conference on Fluidized Bed Combustion.Toronto,Ontario,Canada:ASME,2005:135-146.

[10]YangHairui,ZhangHai,YangShi,et al.Effect of bed pressure  on performance of a CFB boiler[J].Energy & Fuels,2009,23(6):2886-2890.

[11]Bai DR,JinY,Yu ZQ,et al.The axial distribution of the cross-sectionally averaged voidage in fast fluidized beds[J].Powder Technology,1992,71(1):51-58.

[12]LiJinghai,TungY,KwaukM.Axial voidage profiles of fast fluidized beds in different operating regions[M]//Basu P,Large J F.Circulating Fluidized Bed Technology II.Amsterdam:Elsevier,1988:193-203.

[13]XuGuangwen,GaoShiqiu.Necessary parameters for specifying the hydrodynamics of circulating fluidized bed risers—a review and reiteration[J].Powder Technology,2003,137(1-2):63-76.

[14]Lu JF,Zhang JS,Yue GX,et al.Method of calculation of heat transfer coefficient of the heater in a circulating fluidized bed furnace[J].Heat Transfer-Asian Research,2002,31(7):540-550.

[15]LiuXuemin,ZhangMan,LuJunfu,et al.Effect of furnace pressure  on heat transfer in a 135MW CFB boiler[J].Powder Technology,2015,284:19-24.

[16]YangHairui,YueGuangxi,ZhangHai,et al.Updated design and operation experience of CFB boilers with energy saving process in China[R].VGB PowerTech No.7.2011:49-53.

[17]BerrutiF,Pugsley TS,GodfroyL,et al.Hydrodynamics of circulating fluidized bed risers:a review[J].The Canadian Journal of Chemical Engineering,1995,73(5):579-602.

[18]MoXin,WangPeining,YangHairui,et al.A hydrodynamic model for circulating fluidized beds with low riser and tall riser[J].Powder Technology,2015,274:146-153.

[19]杨建华,杨海瑞,岳光溪.循环流化床二次风射流穿透规律的试验研究[J].动力工程,2008,28(4):509-513.YangJianhua,YangHairui,YueGuangxi.Experimental study on secondary air jet penetration in circulating fluidized bed[J].Journal of Power Engineering,2008,28(4):509-513(in Chinese).

[20]LüJunfu,WangQimin,LiYong,et al.Unburned carbon loss in fly ash of CFB boilers burning hard coal[J].Tsinghua Science and Technology,2003,8(6):687-691.

[21]XiaoXianbin,YangHairui,ZhangHai,et al.Research on carbon content in fly ash from circulating fluidized bed boilers[J].Energy & Fuels,2005,19(4):1520-1525.

[22]Yates JG.Fundamentals of fluidized-bed chemical processes[M].London:Butterworths,1983.

[23]Lu JF,Feng JK.On design of CFBC boilers[C]// Proceeding of the 5th International Symposium on Coal Combustion.Nanjing,China,2003:309-313.

[24]YangShi,YangHairui,ZhangHai,et al.Impact of operating conditions on the performance of the external loop in a CFB reactor[J].Chemical Engineering and Processing:Process Intensification,2009,48(4):921-926.

[25]SuJianmin,Hu Nan.Application of fluidization reconstruction energy-saving combustion technology on 300MW CFB boiler[J].Advanced Materials Research,2012,516-517:140-145.

[26]XuGuangwen,NomuraK,GaoShiqiu,et al.More fundamentals of dilute suspension collapse and choking for vertical conveying systems[J].AIChE Journal,2001,47(10):2177-2196.

[27]HuNan,ZhangHai,YangHairui,et al.Effects of riser height and total solids inventory on the gas-solids in an ultra-tall CFB riser[J].Powder Technology,2009,196(1):8-13.

[28]Le GuevelT,ThomasP.Fuel flexibility and petroleum coke combustion at Provence 250 MW CFB[C]// Proceedings of the 17th International Conference on Fluidized Bed Combustion.Jacksonville,Florida,USA:ASME,2003,643-649.

[29]LiJinjing,WangWei,YangHairui,et al.Bed inventory overturn in a circulating fluid bed riser with pant-leg structure[J].Energy & Fuels,2009,23(5):2565-2569.

[30]李金晶,胡南,姚宣,等.裤衩腿型循环流化床炉膛的翻床实验[J].中国矿业大学学报,2011,40(1):54-59.LiJinjing,HuNan,YaoXuan,et al.Experimental study of the bed Inventory overturn in pant-legs furnace of CFB boiler[J].Journal of China University of Mining & Technology,2011,40(1):54-59(in Chinese).

[31]姜华伟,吕俊复,胡南,等.静床高对大截面流化床锅炉床压横向波动影响的模型[J].煤炭学报,2016,41(10):2533-2540.JiangHuawei,LüJunfu,HuNan,et al.Modelling research on effects of static bed height on lateral bed pressure fluctuations in large cross-section circulating fluidized bed boilers[J].Journal of China Coal Society,2016,41(10):2533-2540(in Chinese).

[32]Yue GX,Yang HR,NieL,et al.Hydrodynamics of 300MWe and 600MWe CFB boilers with asymmetric cyclone layout[C]//Proceedings of the 9th International Conference on Circulating Fluidized Beds.Hamburg,2008:153-158.

[33]YangS,Yang HR,LiuQ,et al.Research on flow non-uniformity in main circulation loop of a CFB boiler with multiple cyclones[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustio.Berlin,Heidelberg:Springer,2009:341-344.

[34]MoXin,CaiRunxia,HuangXiaodan,et al.The effects of wall friction and solid acceleration on the mal-distribution of gas-solid flow in double identical parallel cyclones[J].Powder Technology,2015,286:471-477.

[35]Chen XP,Liu DY,Chen ZD,et al.Experimental study on particle feeding and mixing in the bottom zone of a circulating fluidized bed[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:324-329.

[36]LiuDaoyin,ChenXiaoping.Experimental profiles of lateral mixing of feed particles in a three-dimensional fluidized bed[J].AIChE Journal,2011,57(6):1459-1469.

[37]Chen HP,Tian LN,DuQ,et al.Experimental study on coal feeding property of 600MW CFB boiler[C]// Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:453-458.

[38]Liu DY,Chen XP,LiangC,et al.Solids mixing in the bottom zone of fluidized beds[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:459-463

[39]Zhou XL,Cheng LM,Wang QH,et al.Study of air jet penetration in a fluidized bed[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:453-458.

[40]Zhou XL,Cheng LM,Wang QH,et al.Influence of secondary air ratio on gas-solid mixing and combustion in a 300MWe CFB boiler furnace[C]//Proceedings of the 2010 International Conference on E-Product E-Service and E-Entertainment.Henan,China:IEEE,2010:1-4.

[41]DongWeigang,WangWei,LiJinghai.A multiscale mass transfer model for gas-solid riser flows:part 1-sub-grid model and simple tests[J].Chemical Engineering Science,2008,63(10):2798-2810.

[42]DongWeigang,WangWei,LiJinghai.A multiscale mass transfer model for gas-solid riser flows:part II-sub-grid simulation of ozone decomposition[J].Chemical Engineering Science,2008,63(10):2811-2823.

[43]李战国,刘志成,贺军,等.旋风分离器的入口烟道布置对性能的影响[J].中国电机工程学报,2009,29(17):1-7.LiZhanguo,LiuZhicheng,HeJun,et al.Influence of inlet duct layouts on cyclone performance[J].Proceedings of the CSEE,2009,29(17):1-7(in Chinese).

[44]LuJiayi,LuXiaofeng,HeHonghao,et al.Combustion acteristics of the external circulation loop on Baima's 300 MWe circulating fluidized bed boiler[J].Energy & Fuels,2011,25(8):3456-3464.

[45]LuJiayi,LuXiaofeng,LiuHanzhou,et al.Calculation and analysis of dissipation heat loss in large-scale circulating fluidized bed boilers[J].Applied Thermal Engineering,2010,30(13):1839-1844.

[46]Grace JR.Heat transfer in circulating fluidized beds[M]// Basu P.Circulating Fluidized Bed Technology.Amsterdam:Elsevier,1986.

[47]ZhangRuiqing,YangHairui,LuJunfu,et al.Theoretical and experimental analysis of bed-to-wall heat transfer in heat recovery processing[J].Powder Technology,2013,249:186-195.

[48]Andersson BA,LecknerB.Experimental methods of estimating heat transfer in circulating fluidized bed boilers[J].International Journal of Heat and Mass Transfer,1992,35(12):3353-3362.

[49]WangYu,LuJunfu,YangHairui,et al.Measurement of heat transfer in a 465t/h circulating fluidized bed boiler[C]//Proceedings of the 18th International Conference on Fluidized Bed Combustion.Toronto,Ontario,Canada:ASME,2005:327-335.

[50]ZhangRuiqing,YangHairui,ZhangHai,et al.Research on heat transfer inside the furnace of large scale CFB boilers[C]//Proceedings of the 10th International Conference on Fluidized Beds and Fluidization Technology.Sun River,Oregon,USA:ECI,2011:66-74.

[51]WuYuxin,LuJunfu,ZhangJiansheng,et al.Heat Flux and Hydrodynamics of the membrane wall of supercritical pressure circulating fluidized bed boiler[C]//Proceedings of the 5th International Symposium on Multiphase Flow,Heat Mass Transfer and Energy Conversion.Xian,China,2005.

[52]ZhangRuiqing,YangHairui,HuNan,et al.Experimental investigation and model validation of the heat flux profile in a 300 MW CFB boiler[J].Powder Technology,2013,246:31-40.

[53]ZhangP,Lu JF,Yang HR,et al.Heat transfer coefficient distribution in the furnace of a 300MWe CFB boiler[C]// Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:167-171.

[54]潘杰,杨冬,朱探,等.超临界压力水在垂直上升内螺纹管中的传热特性[J].化工学报,2011,62(2):307-314.PanJie,YangDong,ZhuTan,et al.Heat transfer acteristics of supercritical pressure water in vertical upward rifled tube[J].CIESC Journal,2011,62(2):307-314(in Chinese).

[55]潘杰,杨冬,董自春,等.垂直上升光管内超临界水的传热特性试验研究[J].核动力工程,2011,32(1):75-80.PanJie,YangDong,DongZichun,et al.Experimental investigation on heat transfer acteristics of water in vertical upward tube under supercritical pressure[J].Nuclear Power Engineering,2011,32(1):75-80(in Chinese).

[56]李舟航,张大龙,吴玉新,等.垂直上升光管内超临界水的传热恶化分析和判据[J].中国电机工程学报,2014,34(35):6304-6310.LiZhouhang,ZhangDalong,WuYuxin,et al.A new criterion for predicting deterioration of heat transfer to supercritical water in smooth tubes[J].Proceedings of the CSEE,2014,34(35):6304-6310(in Chinese).

[57]LiY,NieL,Hu XK,et al.Structure and performance of a 600MWe supercritical CFB boiler with water cooled panels[C]//Proceedings of the 20th International Conference on Fluidized Bed Combustion.Berlin,Heidelberg:Springer,2009:132-136.

[58]李燕,李文凯,吴玉新,等.带隔墙的600MW超临界循环流化床锅炉水冷壁水动力特性[J].中国电机工程学报,2008,28(29):1-5.LiYian,LiWenkai,WuYuxin,et al.Hydrodynamics of the water wall in a 600 MW supercritical circulating fluidized bed boiler with water cooled panels within the furnace[J].Proceedings of the CSEE,2008,28(29):1-5(in Chinese).

[59]YueG,LingW,LuJ,et al.Development and demonstration of the 600 MW supercritical CFB boiler in Baima power plant[C]//Proceedings of the 22nd International Conference on Fluidized Bed Conversion.Turku,Finland,2015.

[60]GaoM,LiuJ,YueG.Investigation on load control of a 600MW supercritical circulating fluidized bed boiler [C]//Proceedings of the 11st International Conference onFBC.2014,1:711-719.

[61]GaoMingming,ChangTaihua,GaoXiangxiang.Research in data stream clustering based on Gaussian Mixture Model Genetic Algorithm[C]//Proceedings of the 2nd International Conference on Information Science and Engineering.Hangzhou,China,China:IEEE,2010:3904-3907.

[62]吕俊复,张缦,杨海瑞,等.简约型660MW超超临界循环流化床锅炉设计开发[J].中国电机工程学报,2014,34(5):741-747.LüJunfu,ZhangMan,YangHairui,et al.Conceptual design of a simplified 660MW ultra-supercritical circulating fluidized bed boiler[J].Proceedings of the CSEE,2014,34(5):741-747(in Chinese).

[63]蔡润夏,吕俊复,凌文,等.超(超)临界循环流化床锅炉技术的发展[J].中国电力,2016,49(12):1-7.CaiRunxia,LüJunfu,LingWen,et al.Progress of supercritical and ultra-supercritical circulating fluidized bed boiler technology[J].Electric Power,2016,49(12):1-7(in Chinese).

[64]Tullin CJ,GoelS,MoriharaA,et al.Nitrogen oxide(NO and N2O) formation for coal combustion in a fluidized bed:effect of carbon conversion and bed temperature[J].Energy & Fuels,1993,7(6):796-802.

[65]Anthony EJ,Granatstein DJ.Sulfation phenomena in fluidized bed combustion systems[J].Progress in Energy and Combustion Science,2001,27(2):215-236.

[66]LiJingji,YangHairui,WuYuxin,et al.Effects of the Updated National Emission regulation in China on circulating fluidized bed boilers and the solutions to meet them[J].Environmental Science & Technology,2013,47(12):6681-6687.

[67]YueGuangxi,CaiRunxia,LuJunfu,et al.From a CFB reactor to a CFB boiler-the review of R&D progress of CFB coal combustion technology in China[J].Powder Technology,2017,316:18-28.

[68]BasuP.Circulating fluidized bed boilers:design,operation and maintenance[M].Switzerland:Springer,2015.

[69]Fuertes AB,AlvarezD,RubieraF,et al.Surface area and pore size changes during sintering of calcium oxide particles[J].Chemical Engineering Communications,1991,109(1):73-88.

[70]LiuH,Gibbs BM.The influence of calcined limestone on NOx and N2O emissions from  combustion in fluidized bed combustors[J].Fuel,2001,80(9):1211-1215.

[71]Haji-Sulaiman MZ,Scaroni AW.The calcination and sulphation behaviour of sorbents in fluidized bed combustion[J].Fuel,1991,70(2):169-176.

[72]WinterF,WarthaC,LöfflerG,et al.The NO and N2O formation mechanism during devolatilization and  combustion under fluidized-bed conditions[J].Symposium(International) on Combustion,1996,26(2):3325-3334.

[73]Yue GX,Pereira FJ,Sarofim AF,et al.Char nitrogen conversion to NOx in a fluidized bed[J].Combustion Science and Technology,1992,83(4-6):245-256.

[74]HouXiangsong,ZhangHai,YangShi,et al.N2O decomposition over the circulating ashes from coal-fired CFB boilers[J].Chemical Engineering Journal,2008,140(1-3):43-51.

[75]KwaukM,LiJinghai.Fluidization regimes[J].Powder Technology,1996,87(3):193-202.

[76]JinXiaozhong,LuJunfu,YangHairui,et al.Comprehensive mathematical model for coal combustion in a circulating fluidized bed combustor[J].Tsinghua Science and Technology,2001,6(4):319-325.

[77]李竞岌,杨欣华,杨海瑞,等.鼓泡床焦炭型氮氧化物生成的试验与模型研究[J].煤炭学报,2016,41(6):1546-1553.LiJingji,YangXinhua,YangHairui,et al.Experimental study and modeling of NOx generation from  nitrogen in the bubbling bed[J].Journal of China Coal Society,2016,41(6):1546-1553(in Chinese).

[78]张楚,林郁郁,章明川.快速床动力学统一模型Ⅱ:上部稀相与下部浓相固含率的预报[J].工程热物理学报,2012,33(4):694-698.ZhangChu,LinYuyu,ZhangMingchuan.A unified model for fast fluidization dynamics—part II:prediction of upside dilute phase holdup and lower dense phase holdup[J].Journal of Engineering Thermophysics,2012,33(4):694-698(in Chinese).

[79]刘向军,赵燕,徐旭常.循环流化床内煤粉颗粒团燃烧行为理论分析[J].中国电机工程学报,2006,26(1):30-34.LiuXiangjun,ZhaoYan,XuXuchang.Theoretically studies of the coal particle cluster combustion behavior in a circulating fluidized bed[J].Proceedings of the CSEE,2006,26(1):30-34(in Chinese).

[80]Aamand LE,LecknerB.Oxidation of volatile nitrogen compounds during combustion in circulating fluidized bed boilers[J].Energy & Fuels,1991,5(6):809-815.

[81]LiJingji,ZhangMan,YangHairui,et al.The theory and practice of NOx emission control for circulating fluidized bed boilers based on the re-specification of the fluidization state[J].Fuel Processing Technology,2016,150:88-93.