Field test and numerical simulation of banked fire characteristics of supercritical CFB boiler
CPFD method,supercritical CFB boiler,banked fire,bed temperature,pollutant
CFB 锅炉压火过程中,可能会发生料层温度下降快、蓄热少及污染物排放超标等问题,对 电厂的安全、环保以及运行构成威胁。 以 350 MW 超临界 CFB 锅炉为研究对象,对 CFB 锅炉压火 过程进行现场试验和数值模拟。 结果表明:超临界 CFB 锅炉模拟结果与实测数据具有良好的一致 性,模拟准确地预测了炉膛的压力、温度以及气体组分分布,压力平均误差为 5.6%,温度平均误差 为 2.3%,O2 体积分数的平均误差为 6.3%,NOx 质量浓度的平均误差为 5.7%,SO2 质量浓度的平均误 差为 8.5%,验证了数值模型的准确性。 压火过程,锅炉进入密闭状态,O2 体积分数稳定在 19.5%, 床温降至 905 K 后,降温速率为 2 K / min。 炉膛底部床料静止后出现了分层现象,底部床料 85%为 下层床料,下层床料堆积高度约为 1 m。 床料分层影响最大的因素是颗粒粒径,下层为大颗粒床 料,平均颗粒粒径为 1.2 mm,中层为小颗粒床料,平均粒径为 0.5 mm,上层床料所占质量分数仅为 5%,掺杂了大颗粒和小颗粒,颗粒处于悬浮状态,在密闭炉膛内悬浮高度保持不变。 压火时 NOx 质 量浓度与颗粒的体积分数呈负相关,下层床料 NOx 平均质量浓度为 31 mg / m3 ,中层床料 NOx 平均质 量浓度为60mg/m3,上层床料NOx平均质量浓度为121mg/m3。 炉膛进入密闭状态,随着床料回落 完成,SO2 质量浓度保持不变,炉膛上部 SO2 平均质量浓度为 756 mg / m3 ,炉膛下部 SO2 质量浓度同 样受到床料分层影响,上层床料 SO2 质量浓度最高,为 1 680 mg / m3 。 压火过程中炉膛内 NOx 平均 质量浓度约为 100 mg / m3 ,SO2 平均质量浓度约为 1 160 mg / m3 。
In the process of CFB boiler banked fire,some problems may occur,such as fast temperature drop of the material layer,less heat storage,and excessive pollutant discharge. These problems pose a threat to the safety,environmental protection,and operation of a power plant. Taking the 350 MW supercritical CFB boiler as the research object,the field test and numerical simulation of the CFB boiler banked fire process were carried out. The simulation results of the supercritical CFB boiler are in good agreement with the measured data. The simulation can accurately predict the pressure,temperature,and gas component distribution in the furnace. The average errors of pressure,temperature,O 2 concentration,NO x concentration,and SO 2 concentration are 5.6%,2.3%,6.3%,5.7%,and 8.5%,respectively,which verifies the accuracy of the numerical model. [JP+1]During the process of banked fire,the boiler enters the closed state. The oxygen is stable at 19.5%,the bed temperature drops to 905 K,and the cooling rate is 2 K/min. The bed material at the bottom of the furnace is static,and the stratification phenomenon occurs. The bottom bed material with an 85% fraction is the lower bed material,and the accumulation height of the lower bed material is about 1 m. The most influential factor of the bed material stratification is the particle size. The lower layer is large particle bed material,the average particle size is 1.2 mm. The middle layer is small particle bed material,the average particle size is 0.5 mm. The mass fraction of the upper bed material is only 5%,dopes with large and small particles,and particles in a suspension state,in the closed furnace suspension height remains unchanged. The NO x concentration is negatively correlated with the volume fraction of particles. The average NO x concentration of the lower bed material is 31 mg/m 3,the average NO x concentration of the middle bed material is 60 mg/m 3,and the average NO x concentration of the upper bed material is 121 mg/m 3. The furnace enters the closed state,and the SO 2 concentration remains unchanged with the completion of bed material falling back. The average SO 2 concentration in the upper part of the furnace is 756 mg/m 3,while the SO 2 concentration in the lower part of the furnace is also affected by bed material stratification. The SO 2 concentration in the upper bed material is the highest,which is 1 680 mg/m 3. In the process of banked fire,the average concentration of NO x in the furnace is about 100 mg/m 3,and the average concentration of SO 2 is about 1 160 mg/m 3.
主办单位:煤炭科学研究总院有限公司 中国煤炭学会学术期刊工作委员会