超临界循环流化床锅炉深度调峰技术研究与应用Research and application of depth peak regulation technology for supercritical circulating fluidized bed boiler
王虎,范浩东,辛胜伟,张缦,王君峰,邬万竹,杨海瑞,张鹏
WANG Hu,FAN Haodong,XIN Shengwei,ZHANG Man,WANG Junfeng,WU Wanzhu,YANG Hairui,ZHANG Peng
摘要(Abstract):
超临界循环流化床机组深度调峰过程中除了亚临界机组面临的低负荷工况布风板的稳定流化、氮氧化物控制难题外,还涉及水动力的安全性问题。针对超临界循环流化床锅炉深度调峰面临的技术难题,通过流态重构,使临界流化风速降低,保证稳定流化所需的风量减小,同时,减少了炉膛下部燃烧份额,进而减小布风板面积,保证超低负荷流化稳定;开发了垂直管圈二次上升水冷壁工质流程,保证低负荷水动力安全性;降低床料粒度和循环物料粒径,在保证流化和燃烧的前提下,降低一次风比例,强化焦炭颗粒表面的局部还原性气氛,同时对给煤、排渣、送风等布置方式进行优化布置,保证炉内氧量和温度分布均匀,为氮氧化物控制提供保证,最终实现350 MW超临界循环流化床锅炉20%BMCR工况稳定运行,最大壁温偏差为17℃,炉内同层温度偏差在30℃以内。此外,在锅炉从启动到满负荷以及变负荷运行过程中,3个旋风分离器入口烟温的温度偏差始终在10℃以内,氮氧化物全负荷超低排放。
In the process of deep peak regulation of supercritical circulating fluidized bed units, in addition to the problems of stable fluidization of air distribution plate and nitrogen oxide control under low load conditions faced by subcritical units, the safety of hydrodynamics is also involved. In view of the technical problems of deep peak regulation of supercritical circulating fluidized bed boiler, through the reconstruction of flow pattern, the critical fluidization air velocity was reduced, the air volume needed to ensure stable fluidization was reduced, and the combustion share in the lower part of the furnace was reduced. Furthermore, the area of air distribution plate was reduced to ensure the stability of ultra-low load fluidization, and the working fluid flow of secondary rising water wall with vertical tube ring was developed to ensure the hydrodynamic safety of low load. Reduce the particle size of bed material and circulating material, on the premise of ensuring fluidization and combustion, reduce the proportion of primary air, strengthen the local reducing atmosphere on the surface of coke particles, optimize the arrangement of coal feeding, slag discharge and air supply, ensure the uniformity of oxygen and temperature distribution in the furnace, provide a guarantee for the control of nitrogen oxides, and finally realize the stable operation of 350 MW supercritical circulating fluidized bed boiler under 20% BMCR conditions. The maximum wall temperature deviation is 17 ℃,and the temperature deviation of the same layer in the furnace is less than 30 ℃. In addition, in the process of boiler operation from start-up to full load and variable load, the temperature deviation of the inlet flue gas temperature of the three cyclone separators is always within 10 ℃,and the NO_x emission is ultra-low at full load.
关键词(KeyWords):
超临界循环流化床锅炉;深度调峰;流态重构;垂直管圈;低氮燃烧
supercritical circulating fluidized bed boiler;depth peak adjustment;flow pattern reconstruction;vertical tube ring;nitrogen oxides
基金项目(Foundation): 国家重点研发计划资助项目(2019YFE0102100);; 太原市“揭榜挂帅”资助项目
作者(Author):
王虎,范浩东,辛胜伟,张缦,王君峰,邬万竹,杨海瑞,张鹏
WANG Hu,FAN Haodong,XIN Shengwei,ZHANG Man,WANG Junfeng,WU Wanzhu,YANG Hairui,ZHANG Peng
DOI: 10.13226/j.issn.1006-6772.22012502
参考文献(References):
- [1] 柯希玮,张缦,杨海瑞,等.循环流化床锅炉NOx生成和排放特性研究进展[J].中国电机工程学报,2020,40(29):1-13.KE Xiwei,ZHANG Man,YANG Hairui,et al.Research progress on the characteristics of NOx emission in circulating fluidized bed boiler[J].Proceedings of the CSEE,2020,40(29):1-13.
- [2] 孙倩,印江,牛斌,等.300 MW亚临界循环流化床发电机组的全程调峰控制研究[J].电力学报,2020,35(6):522-527.SUN Qian,YIN Jiang,NIU Bin,et al.Research on full-process peak regulation control of 300 MW subcritical circulating fluidized bed generator set[J].Journal of Electric Power,2020,35(6):522-527.
- [3] CATON J A,NARNEY Li J K,CARIAPPA C,et al.The selective non-catalytic reduction of NO using NH3 up to 15% oxygen[J].The Canadian Journal of Chemical Engineering,1995,73:345-350.
- [4] 王鹏程,邓博宇,蔡晋,等.超临界循环流化床锅炉深度调峰技术难点及控制策略[J] .中国电力,2021,4(11):1-8.WANG Pengcheng,DENG Boyu,CAI Jin,et al.Technical points and control strategies on in-depth peak regulation for supercritical circulating fluidized bed boiler[J].Electric Power,2021,4(11):1-8.
- [5] 蔡晋,单露,王志宁,等.超临界350 MW循环流化床锅炉变负荷特性[J].热力发电,2020,49(9):98-108.CAI Jin,SHAN Lu,WANG Zhining,et al.Variable load characteristics of a supercritical 350 MW circulating fluidized bed boiler[J].Thermal Power Generation,2020,49(9):98-108.
- [6] 张缦,张素花,郭学茂,等.流态对CFB燃烧气体污染物排放的影响及其应用[J].工业锅炉,2020,7(3):11-17.ZHANG Man,ZHANG Suhua,GUO Xuemao,et al.The effect and application of solid-gas two-phase flow pattern on the emission in the circulating fluidized bed combustion[J].Industrial Boiler,2020,7(3):11-17.
- [7] IRFAN N.Control of gaseous emissions by flue gas treatment[D].West Yorkshire:The University of Lead,1995.
- [8] 高琴,孔皓,杨海瑞,等.超高参数二次再热循环流化床锅炉技术可行性分析[J].热力发电,2020,49(6):32-37.GAO Qin,KONG Hao,YANG Hairui,et al.Feasibility analysis for ultra-high parameter CFB boiler with secondary reheat[J].Thermal Power Generation,2020,49(6):32-37.
- [9] 刘贤东,吴玉新,张扬,等.循环流化床锅炉循环流率在线测量方法研究[J].洁净煤技术,2020,26(3):9-15.LIU Xiandong,WU Yuxin,ZHANG Yang,et al.Research on in-situ measurement method for ash circulating rate of circulating fluidized bed [J].Clean Coal Technology,2020,26(3):9-15.
- [10] IRFAN N.Flue gas nitrogen oxides control using selective non-catalytic reduction process[J].Pakistan,1997,18(25):175-180.
- [11] 李军,张缦,刘青,等.循环流化床锅炉超低氮氧化物排放理论与实践[J].洁净煤技术,2020,26(3):139-145.LI Jun,ZHANG Man,LIU Qing,et al.Theory and practice of ultra-low NOx emission in circulating fluidized bed boilers [J].Clean Coal Technology ,2020,26(3):139-145.
- [12] 苗苗,孔皓,邓博宇,等.石灰石脱硫对循环流化床锅炉现场试验中N2O排放的影响研究[J].热力发电,2020,49(6):1-6.MIAO Miao,KONG Hao,DENG Boyu,et al.Effect of limestone desulfurization on N2O emission in CFB boiler field test [J].Clean Coal Technology,2020,49(6):1-6.
- [13] 张云.基于流态重构的低能耗循环流化床锅炉技术[J].当代化工研究,2018(12):104-105.ZHANG Yun.Low energy consumption circulating fluidized bed boiler technology based on flow regime reconstruction[J].Chemical Intermediate,2018(12):104-105.
- [14] 葛星垣.基于流态重构的节能超低排放循环流化床锅炉技术[J].机械管理开发,2018,33(5):36-37.GE Xinghuan.Energy saving ultra-low emission circulating fluidized bed boiler technology based on flow pattern reconstruction[J].Mechanical Management and Development,2018,33(5):36-37.
- [15] 柯希玮,蔡润夏,杨海瑞,等.循环流化床燃烧的NOx生成与超低排放[J].中国电机工程学报,2018,38(2):390-396.KE Xiwei,CAI Runxia,YANG Hairui,et al.Formation and ultra-low emission of NOx for circulating fluidized bed combustion[J].Proceedings of the CSEE,2018,38(2):390-396.
- [16] 刘强.CFB锅炉燃烧温度与污染物排放控制技术[J].工业锅炉,2017(5):43-45.LIU Qiang.Combustion temperature and pollutant emission control technology of circulating fluidized bed boiler[J].Industrial Boiler,2017(5):43-45.
- [17] 汪佩宁,蔡润夏,柳成亮,等.300 MWe节能型循环流化床锅炉的设计与运行[J].沈阳工程学院学报(自然科学版),2016,12(4):308-313.WANG Peining,CAI Runxia,LIU Chengliang,et al.Design and operation of 300 MWe energy-saving circulating fluidized bed boiler[J].Journal of Shenyang Institute of Engineering (Natural Science),2016,12(4):308-313.
- [18] 刘雪敏.循环流化床锅炉流态优化对其经济运行的影响[D].北京:清华大学,2016.
- [19] 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.YUE Guangxi,LYU Junfu,XU Peng,et al.Current situation and prospect analysis of circulating fluidized bed combustion[J].China Power,2016,49(1):1-13.
- [20] 李竞岌,杨海瑞,吕俊复,等.节能型循环流化床锅炉低氮氧化物排放的分析[J].燃烧科学与技术,2013,19(4):293-298.LI Jingji,YANG Hairui,LYU Junfu,et al.Low NOx emission characteristic of low energy consumption CFB boilers[J].Journal of Combustion Science and Technology,2013,19(4):293-298.
- [21] 苏建民.基于流态重构的循环流化床锅炉节能燃烧技术的应用实践[J].动力工程学报,2011,31(3):170-175.SU Jianmin.Application practices of energy saving combustion technologies for circulating fluidized bed boiler based on flow pattern reconstruction[J].Journal of Chinese Society of Power Engineering,2011,31(3):170-175.
- 超临界循环流化床锅炉
- 深度调峰
- 流态重构
- 垂直管圈
- 低氮燃烧
supercritical circulating fluidized bed boiler - depth peak adjustment
- flow pattern reconstruction
- vertical tube ring
- nitrogen oxides
- 王虎
- 范浩东
- 辛胜伟
- 张缦
- 王君峰
- 邬万竹
- 杨海瑞
- 张鹏
WANG Hu - FAN Haodong
- XIN Shengwei
- ZHANG Man
- WANG Junfeng
- WU Wanzhu
- YANG Hairui
- ZHANG Peng
- 王虎
- 范浩东
- 辛胜伟
- 张缦
- 王君峰
- 邬万竹
- 杨海瑞
- 张鹏
WANG Hu - FAN Haodong
- XIN Shengwei
- ZHANG Man
- WANG Junfeng
- WU Wanzhu
- YANG Hairui
- ZHANG Peng