600 MW超临界对冲锅炉分级燃烧特性
Staged combustion characteristics of a 600 MW supercritical opposed boiler
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摘要: 为研究超临界燃煤锅炉的燃烧特性,针对 600 MW 对冲旋流燃烧锅炉,利用 CFD(computa-tional fluid dynamics)数值仿真软件研究了分级燃烧超临界锅炉内速度分布、颗粒轨迹分布、温度分布、组分分布特性及 NOx 释放规律。 采用标准 k-ε 模型和拉格朗日随机轨道模型模拟气相湍流流动和气固两相流动;对于固体燃料,借助离散相模型,同时采用非预混燃烧模型模拟煤粉在炉内的燃烧过程;对流项采用二阶迎风格式获得更加精确的物理解;考虑到锅炉炉膛温度高、辐射换热量大,采用P1 辐射模型计算气-气和气-固之间的辐射换热量;对锅炉壁面附近区域的流动传热计算采用标准壁面函数法,节省内存和计算时间。 结果表明:分级对冲燃烧锅炉截面速度呈对称分布,气流充满度好,燃烧稳定;旋流燃烧的方式使炉内出现回流区,加强了炉内气流与煤粉颗粒之间的扰动,强化了传热传质,同时延长了煤粉颗粒在炉内的停留时间;煤粉颗粒的直径影响着煤粉在炉内的燃烧过程,粒径越小,煤粉颗粒在炉内的停留时间越短,影响燃料的燃烧燃尽和锅炉效率,但粒径过大,煤粉颗粒在自身重力作用下落入冷灰斗,影响锅炉的正常安全运行,因此,合适的粒径对炉内燃烧过程十分重要;沿炉膛高度方向,炉内烟气平均温度先上升后下降,在燃尽区补充燃尽风使温度小幅降低,到达炉膛出口截面烟气平均温度约为1100 K;炉内各组分分布规律为:X=11.0935 m 截面,沿炉膛高度方向,O 2 体积分数先上升后下降,CO 2 体积分数逐渐升高,CO 体积分数先上升后下降;分级燃烧使炉内NOx 生成量整体下降,炉膛出口 NO x 浓度约为 385.14 mg/ m 3 。Abstract: In order to study the combustion characteristics of the supercritical coal-fired boilers,the velocity,trajectory of pulverized coal particles,temperature and composition distribution characteristics and NO_x release features during coal combustion in the 600 MW counter-rotating swirling boiler were numerically studied using CFD( Computational Fluid Dynamics) numerical simulation software.The standard k-ε model and lagrangian random orbit model were explored to simulate gas-phase turbulent flow and gas-solid two-phase flow.The solid fuel was simulated by the discrete phase model,besisdes,the pulverized coal combusted in the furnace was simulated by the non-premixed combustion model.The convection term adopted the second order upwind to obtain a more accurate understanding of the matter.Considering the high temperature of the boiler furnace and the large amount of radiation heat transfer,the P1 radiation model was used to calculate the radiation heat transfer between the gas-gas and the gas-solid.The standard wall function method was used to calculated flow heat transfer,which could save the space and calculation time. The results show that the cross-section velocity of the staged combustion boiler is symmetric,the gas flow is full and the combustion is stable.Besides,the symmetrical reflux caused by swirling combustion in the furnace could enhance the disturbance between the gas flow in the furnace and the pulverized coal particles,and then strengthen the heat and mass transfer and increase the residence time of the pulverized coal particles in the furnace.The particle size of pulverized coal in the furnace could affect the combustion process.Specifically,the smaller the particle size the shorter the residence time of pulverized coal particles is in the furnace,which will influence the combustion and burnout of the fuel and the efficiency of the boiler.On the contrary,if the particle size is too large,the pulverized coal particles fall into the ash hopper slagging by their own gravity,and impacts the normal safe operation of the boiler.Therefore,the proper particle size is significantly important for the combustion process in the furnace.The average temperature of the flue gas in the furnace rises and then decreases along the height of the furnace and then reach to about 1 100 K in the cross section of the furnace exit.The temperature in the burnout zone is slightly reduced due to the supplemented over-fire-air.The distribution of various components in the furnace are X = 11.093 5 m section,along the height of the furnace,the volume fraction of O_2 first rises and then decreases,the volume fraction of CO_2 increases gradually,the volume fraction of CO first rises and then decreases,the staged combustion reduces the overall NO_x production,and the concentration of NO_x at the furnace outlet is about 385.14 mg/m~3.
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