氨/煤预热燃烧氮转化特性试验与模拟

Experimental and simulation investigation on nitrogen transformation characteristics in ammonia/coal preheating combustion

  • 摘要: 为解决电站锅炉因空间尺度大,其炉内流场、温度场和浓度场较为无序,易导致氮氧化物(NOx)排放激增从而限制煤氨混燃工程化应用的问题,提出了利用预热燃烧技术促进NH3和煤挥发分氮在预热区提前转化为N2从而降低进入燃烧区燃料氮总量的降氮策略。在自行搭建的电加热式两段沉降炉(drop-tube furnace, DTF)试验系统上考察了预热区过量空气系数(λ1)和混氨比对NO排放及飞灰含碳量的影响,并搭建详细化学反应机理模型对预热燃烧过程中氨氮和煤氮的迁徙转化路径进行了分析。预热燃烧试验和模拟计算结果表明,低预热区过量空气系数工况下,飞灰含碳量随混氨比升高而降低,但NO最大增长幅度超过一倍;此时通过增加预热区过量空气系数可使NO排放增幅逐渐缩小,其原因是氨氮和煤挥发分氮在此过程中向N2的转化率逐渐升高,并最终可达到100%,意味着此时的NO排放仅由焦炭氮的氧化生成量和还原量决定;进一步搭配空气分级可实现20%混氨工况NO排放与纯煤工况相当。预热区化学反应路径分析显示煤热解产物会改变NH3的转化路径,主要体现为促进NH3在CH3等自由基的作用下转化为HCN和HNCO;燃烧区化学反应路径分析则表明碳烟和HO2自由基是还原NO的关键物种。最后对利用开发的新型预热式燃烧器和气化炉预热系统实现氨煤预热燃烧的大型工程化应用进行了展望。

     

    Abstract: The power plant boiler has the characteristics of large spatial scale. The flow field, temperature field and concentration field are disorderly, which is easy to lead to the surge of nitrogen oxide emission so as to limit the engineering application of coal co-firing with NH3. To solve the problem, a de-NOx strategy based on preheating combustion technology was proposed, whose core was to promote the advance conversion of NH3 and volatile-N into N2 in the preheating zone so as to reduce the amount of fuel-N in combustion zone. A two staged drop-tube furnace(DTF) was built to investigate the effects of excess air ratio in preheating zone(λ1) and NH3 proportion on NO emission and unburned carbon content in fly ash. And a detailed chemical reaction mechanism model was built to analyze the transformation path of ammonia nitrogen and coal nitrogen. The results from preheated combustion experiments and simulation calculations showed that, under low λ1 conditions, the unburned carbon content in fly ash decreased as the NH3 proportion increased. However, the maximum increase in NO emissions more than doubled. Increasing λ1 at this stage gradually mitigated the rise in NO emissions. This effect was attributed to the progressive increase in the conversion rate of nitrogen from ammonia and coal volatiles into N2, which could ultimately reach 100%. This indicated that NO emissions under these conditions were determined solely by the balance between the oxidation and reduction of nitrogen in the char. Furthermore, by implementing air staging, NO emissions under a 20% ammonia mixing condition could be comparable to those under pure coal conditions. Chemical reaction pathway analysis in the preheating zone revealed that coal pyrolysis products altered the conversion pathway of NH3, primarily facilitating its transformation into HCN and HNCO through interactions with radicals such as CH3. In the combustion zone, the pathway analysis further identified soot and HO2 radicals as the critical species for NO reduction. Finally, the large-scale engineering application of coal co-firing with ammonia preheating combustion by using the developed new preheating burner and gasifier preheating system was forecasted.

     

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