Research on large proportion of coal slime co-combustion in a 300 MW CFB boiler
ZHANG Ping;CHEN Lujian;JIANG Hua;ZHANG Man;XU Wei;LIU Shi;YANG Hairui;LYU Junfu;
Abstract:
Large proportion of coal slime co-combustion in CFB boilers is an effective means to treat low quality coal such as coal slime. A one-dimensional chamber model was used to simulate the operating conditions of a CFB boiler with different proportions of coal slime co-combustion. The effects of blended coal slime ratio on the average particle size in CFB boiler furnace,the residence time of particle in furnace and the material concentration of upper furnace were studied,and the optimal operation condition on flow regime under the condition of large proportion of coal slime was determined. The simulation results show that increasing the proportion of coal slime can increase the material circulation flow rate and the residence time of particles in the intermediate size range( 0.1-0.3 mm) in the furnace,and improve the burnout rate of fuel. Increasing the proportion of coal slime can increase the particle concentration of upper furnace,which is beneficial to improve the heat transfer in the upper part of the furnace,reduce the temperature of the furnace,and control pollutants.Based on the operation data of large proportion of coal slime co-combustion in a 300 MW circulating fluidized bed boiler unit in Panbei Power Plant,the effects of proportion of coal slime co-combustion on bed temperature,exhaust gas temperature,carbon content of bottom slag and fly ash were analyzed. When the boiler load is at 300 MW,the bed temperature obviously decreases after the blended coal slime being burned,the carbon content of the fly ash and the smoke exhaust temperature increase with the proportion of blended coal slime increased,and the carbon content of the bottom slag decreases with the proportion of blended coal slime increased. In order to achieve the goal of large proportion of coal slime co-combustion,it is recommended to control the coal particle size of gangue,and it is necessary to strengthen the tail soot blowing or adjust the tail heating surface appropriately.
Key Words: CFB;large proportion;coal slime;co-combustion;material balance
Foundation: 国家重点研发计划资助项目(2016YFB0600203)
Authors: ZHANG Ping;CHEN Lujian;JIANG Hua;ZHANG Man;XU Wei;LIU Shi;YANG Hairui;LYU Junfu;
DOI: 10.13226/j.issn.1006-6772.19103101
References:
- [1]中华人民共和国统计局.中国统计年鉴[M].北京:中国统计出版社,2018.Statistics Bureau of the People's Republic of China. China statistical yearbook[M]. Beijing:China Statistics Press,2018.
- [2]裴婷.煤泥燃烧过程的试验研究[D].徐州:中国矿业大学,2016:1-2.PEI Ting. Experimental study on combustion process of coal slime[D]. Xuzhou:China University of Mining and Technology,2016:1-2.
- [3]冯俊凯,岳光溪,吕俊复.循环流化床燃烧锅炉[M].北京:中国电力出版社,2003:24-38.FENG Junkai,YUE Guangxi,LYU Junfu. Circulating fluidized bed combustion boiler[M]. Beijing:China Electric Power Press,2003:24-38.
- [4]邵伟,袁隆基,郭晓勇,等.440 t/h循环流化床锅炉大比例掺烧煤泥试验研究[J].热力发电,2013,42(4):89-93.SHAO Wei,YUANLongji,GUO Xiaoying,et al. Experimental study on large proportion coal slurry co-firing in a 440t/h CFB boiler[J]. Thermal Power Generation,2013,42(4):89-93.
- [5]刘彦鹏,李建民,余永生,等.300MW循环流化床锅炉掺烧煤泥试验研究[J].热力发电,2010,39(10):60-64.LIU Yanpeng,LI Jianmin,YU Yongsheng,et al. Test study on mixedly burning coal slime in 300MW CFB boiler[J]. Thermal Power Generation,2010,39(10):60-64.
- [6]刘吉堂,王冬梅,蒋文斌,等.大型CFB锅炉大比例掺烧煤泥的分析[J].电力技术,2010,19(10):52-57.LIU Jitang,WANG Dongmei,JIANG Wenbin,et al. Analysis on the large circulating fluidized bed boiler firing peat as mean fuel[J].Electric Power Technology,2010,19(10):52-57.
- [7]杨海瑞.循环流化床锅炉物料平衡研究[D].北京:清华大学,2003:17-21.YANG Hairui. Research on mass balance in circulating fluidized bed boiler[D]. Beijing:Tsinghua University,2003:17-21.
- [8]杨海瑞,肖显斌,岳光溪.循环流化床锅炉内的灰平衡模型研究[J].煤炭转化,2002,25(3):59-64.YANG Hairui,XIAO Xianbin,YUE Guangxi. Modeling of ash balance in CFB boiler[J]. Coal Conversion,2002,25(3):59-64.
- [9] YANG H,YUE G,XIAO X,et al. 1D modeling on the material balance in CFB boiler[J]. Chemical Engineering Science,2005,60(20):5603-5611.
- [10] YUE G,WANG L,LI Y,et al. Ash size formation characteristics in CFB coal combustion[C]//Proc. of 4th Int. Conference on Circulating Fluidized Beds. Somerset:[s.n.],1993:110-115.
- [11]唐治.流化床燃烧条件下煤的成灰特性实验研究[D].北京:清华大学,2001:4-12.TANG Zhi. Experimental study on the ash formation behavior of coal under the condition of fluidized bed combustion[D]. Beijing:Tsinghua University,2001:4-12.
- [12]杨海瑞,肖显斌,吕俊复,等.CFB锅炉内成灰特性的实验研究方法[J].化工学报,2003,54(8):1183-1187.YANG Hairui,XIAO Xianbin,LYU Junfu,et al. Experimental technique on coal ash formation in CFB combustion[J]. Journal of ChemicalIndustry andEngineering,2003,54(8):1183-1187.
- [13] ZHANG Yi,ZHANG Man,ZHU Shahong,et al. Mechanism analysis of gas solid flow non-uniformity problem of 330 MW CFB boiler[J]. Chemical Engineering Research and Design,2019,145:258-267.
- [14] YUE G X,LU J F,ZHANG H,et al. Design theory of circulating fluidized bed boilers[C]//Proceedings of 18th international conference on fluidized bed combustion. Toronto:[s.n.],2005.
- [15] CAI Runxia,ZHANG Hai,ZHANG Man,et al. Development and application of the design principle of fluidization state specification in CFB coal combustion[J]. Fuel Processing Technology,2018,174:41-52.
- [16]杨婷婷,邸小慧,洪烽,等.掺烧煤泥循环流化床锅炉床温动态建模[J].热力发电,2018,47(2):43-48.YANG Tingting,DI Xiaohui,HONG Feng,et al. Dynamic modeling for bed temperature of circulating fluidized bed bilersco-firing coal slime[J]. Thermal Power Generation,2018,47(2):43-48.
- ZHANG Ping
- CHEN Lujian
- JIANG Hua
- ZHANG Man
- XU Wei
- LIU Shi
- YANG Hairui
- LYU Junfu
- Guotou Panjiang Power Generation Co.
- Ltd.
- State Key Laboratory of Power Systems
- Department of Energy and Power Engineering
- Tsinghua University
- ZHANG Ping
- CHEN Lujian
- JIANG Hua
- ZHANG Man
- XU Wei
- LIU Shi
- YANG Hairui
- LYU Junfu
- Guotou Panjiang Power Generation Co.
- Ltd.
- State Key Laboratory of Power Systems
- Department of Energy and Power Engineering
- Tsinghua University