工业规模循环流化床锅炉煤与木屑共燃烧的欧拉-欧拉多流体模拟

Vasujeet Singh, Pruthiviraj Nemalipuri, Harish Chandra Das, Vivek Vitankar
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引用次数: 0

摘要

煤和生物质的混合燃烧减少了二氧化碳的净排放量。流化床技术最适合燃烧生物质和煤组合,而不需要对燃烧系统进行重大修改。大型循环流化床锅炉试验既不经济又费时。在过去的几十年里,数学建模已经获得了知名度,并允许研究人员探索不同的情况和设计优化。目前的研究提出了工业规模CFBC锅炉的数学模型(165 TPH CFBC锅炉100 MWe CPP)在印度奥里萨邦的Hindalco工业公司运行,使用煤和木屑生物质(90%煤+ 10%木屑)共燃烧。模拟采用欧拉-欧拉多流体模型,考虑了四种不同的欧拉相(煤、锯末、砂和混合气)。利用颗粒流动动力学理论(KTGF)模拟了床层物料与燃料颗粒之间的碰撞。采用用户定义函数(用C语言编写)来模拟非均相化学反应的反应动力学。数值方法与现场工业数据的压降、流化床高度、悬浮密度、床层空隙和温度变化进行了验证。结果部分介绍了单独使用煤和混合燃料时的压降、流化床高度、轴向速度分布、砂和混合气体温度变化、气体成分和污染物排放(二氧化硫和氧化亚氮)的比较。流体力学稳态分析揭示了砂粒在锅炉流化床区的再循环。结果表明,10%木屑与90%煤混合燃烧后,锅炉出口压降降低11.42%,氧质量分数提高13.17%,一氧化二碳质量分数降低10.63%,二氧化二硫质量分数降低16.26%,氧化亚氮质量分数降低7.17%。
本文章由计算机程序翻译,如有差异,请以英文原文为准。

An Eulerian-Eulerian multifluid simulation for co-combustion of coal and sawdust in industrial scale circulating fluidized bed boiler

An Eulerian-Eulerian multifluid simulation for co-combustion of coal and sawdust in industrial scale circulating fluidized bed boiler
Co-combustion of coal and biomass reduced the net Carbon di-oxide emissions. The fluidized bed technology is best suited to burn biomass and coal combinations without major modifications to the combustion systems. Experimentation of large-scale CFBC boilers is uneconomical and time-consuming. Mathematical modelling has gained visibility in the last several decades and allows researchers to explore different circumstances and design optimization. The current research presents mathematical modelling of an industrial scale CFBC boiler (165 TPH CFBC Boiler for 100 MWe CPP) functioning in Hindalco Industries, Odisha, India, using co-combustion of coal and sawdust biomass (90 % coal + 10 % sawdust). The simulation is performed using the Eulerian-Eulerian multifluid model by considering the four different Eulerian phases (coal, sawdust, sand, and mixture gas). The kinetic theory of granular (KTGF) flows is used to model the collisions between bed material and fuel particles. User-defined functions (written in C programming language) are employed to model the reaction kinetics of heterogeneous chemical reactions. The numerical methodology is validated with the onsite industrial data of pressure drop, fluidized bed height, suspension density, bed voidage, and temperature variations. The comparison of pressure drop, fluidized bed height, axial velocity profiles, sand and mixture gas temperature variations, gas compositions, and pollutant emissions (Sulfur di-oxide and nitrous oxide) using solo coal and blended fuel are presented in the result section. Hydrodynamics steady reveals the recirculation of sand particles in the fluidized bed region of the boiler. The comparison of solo coal and blended fuel combustion study reveals an 11.42 % reduction in pressure drop, 13.17 % increase in oxygen mass fraction, 10.63 % reduction in carbon mono oxide mass fraction, 16.26 % reduction in Sulfur di-oxide mass fraction, and 7.17 % reduction in nitrous oxide mass fraction is observed at the boiler outlet while using the 10 % sawdust blends with 90 % coal.
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