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粉煤和石灰石加入位置对循环流化床燃煤过程NOx与N2O排放的影响
引用本文:张磊,杨学民,谢建军,丁同利,姚建中,宋文立,林伟刚. 粉煤和石灰石加入位置对循环流化床燃煤过程NOx与N2O排放的影响[J]. 中国电机工程学报, 2006, 26(21): 0-98
作者姓名:张磊  杨学民  谢建军  丁同利  姚建中  宋文立  林伟刚
作者单位:中国科学院过程工程研究所,北京市,海淀区,100080
基金项目:国家自然科学基金重点项目(90210034),国家自然科学基金项目(50576101),国家自然科学基金委创新研究群体基金项目(20221603)~~
摘    要:在30kW的循环流化床(CFB)上进行3种煤的燃烧实验,考察了粉煤和脱硫剂加入位置、分级燃烧以及空气过剩系数对NOX和N2O排放的影响。所采用的CFB燃煤系统由提升管和下行床构成,提升管主要用于粉煤燃烧,下行床主要用于固体床料循环和粉煤热解。粉煤或脱硫剂分别自传统的一次空气布风板上方和下行床上部两个位置加入。结果表明,在不加脱硫剂的条件下,降低空气过剩系数和一次空气化学计量比均可有效降低NO排放,但对N2O排放则呈现上升、下降和无明显变化多种趋势。当粉煤加入位置自传统的提升管下部改变到下行床上部时,减少空气过剩系数或减少一次空气化学计量比可明显降低其中两种煤的NO排放,并可少量降低另一种煤N2O的排放;从下行床加入粉煤时,空气分级和低O2燃烧对NO排放的影响程度有所减弱。最后,对一种煤进行了脱硫实验,随Ca/S摩尔比的升高,SO2排放显著降低,NO排放升高,而N2O则先上升后下降;且自下行床加入时,NO排放更低;CaCO3加入位置变化对N2O排放无明显影响。

关 键 词:热能动力工程  煤燃烧  循环流化床  加入位置  NO  N2O
文章编号:0258-8013(2006)21-0092-07
收稿时间:2006-05-21
修稿时间:2006-05-21

Effect of Coal and Limestone Addition Position on Emission of NOx and N2O during Coal Combustion in a Circulating Fluidized Bed Combustor
ZHANG Lei,YANG Xue-min,XIE Jian-jun,DING Tong-li,YAO Jian-zhong,SONG Wen-li,LIN Wei-gang. Effect of Coal and Limestone Addition Position on Emission of NOx and N2O during Coal Combustion in a Circulating Fluidized Bed Combustor[J]. Proceedings of the CSEE, 2006, 26(21): 0-98
Authors:ZHANG Lei  YANG Xue-min  XIE Jian-jun  DING Tong-li  YAO Jian-zhong  SONG Wen-li  LIN Wei-gang
Affiliation:Institute of Process Engineering, Chinese Academy of Sciences, Haidian District, Beijing 100080, China
Abstract:The effects of coal and limestone addition at different positions on NOx and N2O emissions from a 30kW scale coal-fired circulating fluidized bed (CFB) were investigated. Both staging combustion and excess air number were studied in this paper. Three coals from western China were applied. The CFB combustor consists of a riser and a downer, which the riser was designed as coal combustor and the downer was used to the circulation of solid material and coal pyrolysis. Two addition port of were adopted for coal or limestone in this study, which was located 20mm above the primary air distributor in the riser and the other was at the upper of the downer. The results show that, without limestone addition Port, coal being injected through the two addition port, reducing first air stoichiometry or excess air number always results in the decrease of NO emissions for the three coals. However, its effects on N2O emissions are not uniform. With the increase of excess air number, N2O emissions increase, decrease and no obvious variation all can be observed. And the effects of air staging on N2O emissions are not obvious. The switch of coal addition port from the riser to the downer, always but not ever, leads to the reduction of NO emissions, but its effect on N2O emissions is much smaller. The effects of the first air stoichiometry and excess air number on NO emissions, compared with being added into the riser, will be weaken when coals were added into the downer. One of the three coals was adopted to investigate the influence of limestone on emissions of SO2 and nitrogen oxides. The results show that SO2 emissions decrease, NO emissions increase and N2O emissions firstly increase slightly and then decrease with the increase ofCa/S molar ratio. Compared with being added into the riser, the limestone added into the downer can result in a smaller increase of NO emissions. However, the switch of limestone addition port has no significant effect on N2O emissions.
Keywords:thermal power engineering  coal combustion  circulating fluidized bed  coal addition position  NO  N2O
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