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    200MW富氧燃烧锅炉配风优化数值模拟研究

    Numerical Simulation on Optimization of Air Distribution Mode for a 200 MW Oxy-fuel Combustion Boiler

    • 摘要: 以200 MW四角切圆煤粉锅炉为研究对象,采用CFD软件结合改进的辐射特性模型以及化学反应机理,对煤粉空气燃烧工况及不同氧气体积分数下的富氧燃烧工况进行了数值模拟,通过研究炉内的燃烧及传热特性,对富氧燃烧工况进行了配风优化设计。结果表明:在富氧燃烧干循环工况下炉内出现高体积分数的CO;干、湿循环工况的入炉氧气体积分数分别为28.5%和27.1%时,炉膛的总辐射传热量与空气燃烧工况几乎相同;提高下二次风的动量能有效减小冷灰斗区域的CO体积分数,采用偏转二次风技术能有效减弱壁面附近的还原性气氛。

       

      Abstract: Taking a 200 MW tangentially-fired boiler as an object of study, numerical simulations were conducted on the pulverized coal combustion process respectively in pure air and oxy-fuel environment, by the computational fluid dynamics (CFD) combined with improved radiation model and chemical reaction mechanism. Based on analysis of the in-furnace combustion and heat transfer characteristics, the oxy-fuel combustion condition was optimized. Results show that high concentrations of CO tend to appear in dry flue gas recycling; the total radiative heat transfer in oxy-fuel combustion with 28.5% and 27.1% concentration of oxygen respectively under dry and wet flue gas recycling mode is nearly the same as that in pure air combustion; increasing the momentum of secondary air (SA) can effectively reduce the concentration of CO in the hopper area, and the utilization of SA deflection technology can effectively weaken the reducing atmosphere near the wall.

       

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