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氨/煤气流床半气化燃烧及氮转化特性实验研究

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氨气(NH3)作为零碳富氢燃料,在燃煤锅炉中掺烧NH3 是从燃烧源减少碳排放的有效途径,但会带来NOx排放升高和煤粉燃尽变差等问题.为实现燃煤锅炉掺烧NH3 的低NOx排放,在自行搭建的气流床半气化燃烧实验台上探究了气化炉掺烧 20%的NH3(G-20%NH3)和燃烧室掺烧 20%的NH3(C-20%NH3)中燃料氮的转化和NOx排放特性.研究发现,气化炉内掺烧NH3 会降低炉膛温度,但对煤粉的气化反应影响较小,与纯煤工况相比,煤氮的转化率仅降低了 3.64%,挥发分和固定碳转化率分别仅降低了 0.70%和 2.54%.在气化炉掺烧NH3 中,NH3 在气化炉中的转化率可达69.55%.气化炉内总燃料氮向N2 的转化率为68.88%,其中NH3-N向N2 的转化率为67.73%.同时,气化炉掺烧NH3 促进了煤-N和NH3-N向HCN的转化,转化率为 0.36%.气化炉中煤粉的热解促进了NH3 的热解,相较于纯煤,气化炉掺烧NH3 使气化炉出口H2 体积分数升高了69.23%.掺烧NH3 降低了燃烧室燃烧初期的温度分布.相较于纯煤,气化炉和燃烧室掺烧NH3 使燃烧室的温度峰值分别降低了 46℃和 62℃.但是,掺烧NH3 推迟了气化半焦的燃烧,增加了燃尽区的温度.气化炉和燃烧室掺烧NH3 中燃尽区平均温度比纯煤工况分别升高了 135.8℃和 72.8℃,促进了煤粉的燃尽.其中燃烧室掺烧NH3 的促进效果更为显著,相较于纯煤,C-20%NH3 中飞灰含碳降低了 1.8%.但气化炉掺烧NH3 更有利于降低NOx排放,相较于C-20%NH3,G-20%NH3 的NO排放降低了23.51%.
An experimental study on the characteristics of ammonia/coal mild gasification-combustion and the Fuel-N transformation
Ammonia(NH3)is a carbon-free and hydrogen-rich fuel.NH3 co-firing in coal-fired boiler is an effective ap-proach to reduce carbon emissions from the combustion source.However,it can lead to problems such as high NOx emis-sions and poor coal burnout.To address the issues above,this paper investigated the Fuel-N conversion and NOx emis-sions during co-firing 20%NH3 in gasifier(G-20%NH3)and in combustor(C-20%NH3)using a self-built mild gasification-combustion experimental rig.The research found that the co-firing NH3 in the gasifier can decrease the gasifier temperat-ure.However,it has little effect on the coal gasification reactions in gasifier.Compared with a pure coal condition,the conversion ratio of coal-nitrogen was only reduced by 3.64%,and the conversion ratio of volatile matter and fixed carbon decreased by only 0.70%and 2.54%,respectively.Besides,the conversion of NH3 in the gasifier can reach 69.55%during the condition of G-20%NH3.The 68.88%of total fuel-N was conversed to N2 in the gasifier,with NH3-N converting to N2 was 67.73%in G-20%NH3.In addition,the NH3 co-firing in the gasifier promoted the transformation of coal-N and NH3-N to HCN,with the value of 0.36%.Moreover,the coal pyrolysis in the gasifier promoted the NH3 pyrolysis.Compared with pure coal,the NH3 co-firing in the gasifier increased the H2 concentration at the outlet of the gasifier by 69.23%than that of pure coal.The NH3 co-firing also decreased the temperature during the preliminary stage of combustion.Com-pared with pure coal,the NH3 co-firing in the gasifier and combustor decreased the temperature peak by 46℃and 62℃,respectively.Simultaneously,the NH3 co-firing delayed the occurrence of temperature peaks.Additionally,the NH3 co-fir-ing delayed the gasified char combustion in the combustor.The average temperature in the burnout zone increased by 135.8℃and 72.8℃during G-20%NH3 and C-20%NH3,respectively,compared to PC.It was more conducive to the burnout of pulverized coal.The NH3-cofiring in combustor had more significant promoting effects on the burnout of pul-verized coal,in which the unburned carbon in fly ash decreased by 1.8%compared PC.However,the NH3 co-firing in gas-ifier was more effective in reducing NOx emissions.During the G-20%NH3,NO emissions were decreased by 23.51%compared to C-20%NH3.The study offers some innovative ideas and data reference for the development of low NOx emis-sion technology for NH3 co-firing in coal-fired boiler.

ammonia/coal co-firingmild gasification-combustion characteristicsfuel-N transformationNOx emis-sion

崔保崇、王肖肖、舒逸翔、林辉、谭厚章、王学斌

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西安交通大学热流科学与工程教育部重点实验室,陕西西安 710049

氨/煤混燃 半气化-燃烧特性 燃料氮转化 NOx排放特性

国家重点研发计划资助项目

2022YFB4100500

2024

煤炭学报
中国煤炭学会

煤炭学报

CSTPCD北大核心
影响因子:3.013
ISSN:0253-9993
年,卷(期):2024.49(10)