烟气再循环与空气分级对氢氧化铝焙烧炉运行参数的影响Effects of flue gas recirculation and air staging on the operating parameters of aluminum hydroxide calciner
李潇峰,邹俊,张扬,王志宁,张海,吕俊复,刘青,张守玉
LI Xiaofeng,ZOU Jun,ZHANG Yang,WANG Zhining,ZHANG Hai,LYU Junfu,LIU Qing,ZHANG Shouyu
摘要(Abstract):
氢氧化铝焙烧炉常用SCR或SNCR技术降低NO_x排放,但存在催化剂被污染以及氨逃逸等问题,亟待发展一条新的减排方案。烟气再循环和空气分级技术是降低氢氧化铝气态悬浮焙烧炉NO_x排放的潜在手段,但烟气再循环和空气分级燃烧技术对气态悬浮焙烧炉运行参数的影响规律仍不明确。以3 000 t/d规模的氢氧化铝气态悬浮焙烧炉系统为研究对象,研究了烟气再循环和空气分级对氢氧化铝气态悬浮焙烧炉运行参数的影响规律。通过计算发现,当烟气再循环率为20%时,系统总过量空气系数降低至1.1左右,可维持较大的一次风量,保证悬浮焙烧状态的同时,使主焙烧炉(P04)下部达到欠氧还原性气氛,进而抑制NO_x的生成。烟气再循环率在20%且空气分级的燃尽风率在25%以内时,GSC炉系统中各分离器效率变化可忽略。GSC炉系统增加烟气再循环和空气分级后,若不调整燃料分配,焙烧温度会降低,可能对氧化铝产品质量产生不利影响。通过优化GSC炉的燃料分配,可显著降低烟气再循环和空气分级对系统运行参数的影响程度。烟气再循环达20%且空气分级的燃尽风率在25%时,优化后的GSC炉系统仍可在保证氢氧化铝焙烧工艺温度和整体热效率的情况下,实现主焙烧炉膛下部的欠氧还原性燃烧气氛,为GSC焙烧炉的低氮燃烧设计提供了必要条件。
SCR and SNCR technology are commonly used to reduce NO_x emission of aluminum hydroxide gaseous suspension calciners(GSC). However,due to the problems of contamination on catalyst and ammonia slip,it is urgent to develop a new scheme to reduce NO_x emission. Fuel gas recirculation and air staged combustion are potential approaches to reduce NO_x emissions of aluminum hydroxide GSC.However,the effects of fuel gas recirculation and air staging on operating parameters of GSC are still unclear. In the present study,taking a 3 000 t/d aluminum hydroxide GSC as the research object,the effects of the flue gas recirculation and air staging on the GSC operating parameters were investigated. It is found that when the flue gas recirculation rate is 20%,the total excess air ratio of the system is reduced to about 1.1,which can maintain a large primary air volume,ensure the suspension roasting state,and make the lower part of the main roasting furnace( P04) achieve a reductive atmosphere,thus inhibiting the formation of NO_x. The changes in the separation efficiency of each cyclone in GSC caused by the flue gas recirculation and air staging ware negligible when the flue gas recirculation ratio are below 20% and the over fire air ratio of the air staged combustion are below 25%. The flue gas recirculation and air staged combustion result in a decrease of the calcination temperature if the fuel distribution is not well adjusted,which may have adverse effects on the quality of alumina products. However,by optimizing fuel distribution of the GSC calciner,the influence of flue gas recirculation and air staging on operating parameters can be largely reduced. When the flue gas recirculation ratio reaches 20% and the over fire air ratio reaches 25%,the lower part of the main furnace of the GSC calciner can achieve a reductive atmosphere while the aluminum hydroxide calcination temperature and overall thermal efficiency are still ensured,which provides the necessary condition for the low-NO_xcombustion design of the GSC process.
关键词(KeyWords):
气态悬浮焙烧炉;烟气再循环;空气分级;物料平衡;热平衡
gas suspension calciner;flue gas recirculation;air staging;material mass balance;heat balance
基金项目(Foundation): 国家自然科学基金资助项目(51706119);; 四川省科技计划资助项目(2018JZ0021,2019YFS04976)
作者(Author):
李潇峰,邹俊,张扬,王志宁,张海,吕俊复,刘青,张守玉
LI Xiaofeng,ZOU Jun,ZHANG Yang,WANG Zhining,ZHANG Hai,LYU Junfu,LIU Qing,ZHANG Shouyu
DOI: 10.13226/j.issn.1006-6772.IF20081002
参考文献(References):
- [1]毕诗文,于海燕.氧化铝生产工艺[M].北京:化学工业出版,2005.BI Shiwen.Production process of alumina[M].Beijing:Chemical Industry Press Co.,Ltd.,2005.
- [2]环境保护部.铝工业污染物排放标准:GB 25465-2010[S].北京:中国环境科学出版社,2010.Ministry of Ecology and Environment of the People's Republic of China.Emission standard for pollutants from aluminum industry:GB 25465-2010[S].Beijing:China Environment Publishing Group,2010.
- [3]徐良策.低氮燃烧脱硝技术在氧化铝焙烧炉的应用[J].中国金属通报,2019(8):9-10.XU Liangce.Application of low nitrogen combustion denitration technology in alumina roaster[J].China Metal Bulletin,2019(8):9-10.
- [4]尹海滨,崔士龙.氧化铝焙烧炉烟气脱硝技术的分析及建议[J].中国环保产业,2017(9):47-49.YIN Haibin,CUI Shilong.Analysis and suggestion on flue gas denitration technology in baking furnace of alumina[J].China Environmental Protection Industry,2017(9):47-49.
- [5]黄耀.循环流化床气化炉煤气脱氨技术浅析[J].有色金属设计,2019,46(2):40-42,60.HUANG Yao.Abrief analysis on ammonia removal technology for circulating fluidized bed coal gasifier[J].Nonferrous Metals Design,2019,46(2):40-42,60.
- [6]杨协和,蔡润夏,张扬,等.空气分级技术对焙烧炉内煤气燃烧NOx生成的影响[J].洁净煤技术,2019,25(3):75-81.YANG Xiehe,CAI Runxia,ZHANG Yang,et al.Effect of air grading technology on NOxformation of coal gas combustion in a calciner[J].Clean Coal Technology,2019,25(3):75-81.
- [7]桑海波.氢氧化铝焙烧炉烟气脱硝技术探析[J].世界有色金属,2019(18):8-9.SANG Haibo.Study on technology for denitrification of hydtatio calciner flue gas[J].World Nonferrous Metals,2019 (18):8-9.
- [8]胡满银,乔欢,杜欣,等.烟气再循环对炉内氮氧化物生成影响的数值模拟[J].华北电力大学学报(自然科学版),2007,34(6):77-82.HU Manyin,QIAO Huan,DU Xin,et al.Numerical simulations of the influence of flue gas recycle on nitrogen oxide formation in boiler[J].Journal of North China Electric Power University (Natural Science Edition),2007,34(6):77-82.
- [9]JOO Baltasar,MARIA G Carvalho,PEDRO Coelho,et al.Flue gas recirculation in a gas-fired laboratory furnace:Measurements and modelling[J].Fuel,1997,76(10):919-929.
- [10]谢正武,梁海杰,车得福.烟气再循环的作用及其对锅炉热力计算的影响[J].能源研究与信息,1999(3):42-48.XIE Zhengwu,LIANG Haijie,CHE Defu.The function of the gas recirculation of boilers and its effect on thermal calculation[J].Energy Research and Information,1999(3):42-48.
- [11]LIU Jun,LUO Xiaoyu,YAO Sheng,et al.Influence of flue gas recirculation on the performance of incinerator-waste heat boiler and NOxemission in a 500 t/d waste-to-energy plant[J].Waste Management,2020,105:450-456.
- [12]ZHANG Xiaohui,FENG Peng,XU Jiarui,et al.Numerical research on combining flue gas recirculation sintering and fuel layered distribution sintering in the iron ore sintering process[J].Energy,2020,192:1-11.
- [13]王杰刚,皇雅斌,魏博,等.基于迭代的注汽锅炉烟气再循环热力参数计算及对燃烧的影响[J].石油石化绿色低碳,2019,4(3):51-56.WANG Jiegang,HUANG Yabin,WEI Bo,et al.Iterationcalculation of FGR thermodynamic parameters in steam injection boiler and effect on combustion[J].Green Petroleum&Petrochemicals,2019,4(3):51-56.
- [14]孙俊威,戴维葆,阎维平,等.不同烟气再循环方案对1 000 MW超超临界二次再热锅炉的影响[J].热能动力工程,2019,34(5):49-56.SUN Junwei,DAI Weibao,YAN Weiping,et al.Influence of different flue gas recirculation schemes on 1 000 MW ultra-supercritical double reheat boiler[J].Journal of Engineering for Thermal Energy and Power,2019,34(5):49-56.
- [15]汪丽芬,王恩禄,刘磊,等.富氧燃烧锅炉热平衡计算方法研究[J].锅炉技术,2014,45(1):31-36.WANG Lifen,WANG Enlu,LIU Lei,et al.Research on the heat balance calculation method of the oxy fuel combustion boilers[J].Boiler Technology,2014,45(1):31-36.
- [16]梅炽,王临江,周孑民,等.有色冶金炉设计手册[M].北京:冶金工业出版社,2000:475-497.MEI Zhi,WANG Linjiang,ZHOU Jiemin,et al.Design Manual of non-ferrous metallurgical furnace[M].Beijing:Metallurgical Industry Press Co.,Ltd.,2000:475-497.
- [17]A.C.霍夫曼,L.E.斯坦因.旋风分离器:原理、设计和工程应用[M].北京:化学工业出版社,2004:82.HOFFMANN Alex C,STEIN Louis E.Cyclone separators:Principles,design and engineering applications[M].Beijing:Chemical Industry Press Co.,Ltd.,2004:82.
- [18]许圣华.烟气物性的直接计算方法[J].苏州丝绸工学院学报,1999,19(3):32-36.XU Shenghua.Direct calculation of flue gas properties[J].Journal of Soochow University (Engineering Science Edition),1999,19(3):32-36.
- 气态悬浮焙烧炉
- 烟气再循环
- 空气分级
- 物料平衡
- 热平衡
gas suspension calciner - flue gas recirculation
- air staging
- material mass balance
- heat balance