低氮氧化物锅炉燃烧器燃料诱导烟气再循环(FIR)系统的性能优化

Michael A. Lorra, Joseph D. Smith, W. Bussman, T. L. Webster
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引用次数: 1

摘要

新的燃烧器设计技术是利用燃料气体喷射的动量夹带烟气,以稀释可燃混合物,以减少氮氧化物的排放。利用导烟器,这些设计从炉堆的对流部分上方夹带烟气,并与导烟器下游的燃料混合。这种稀释的烟气/燃料混合物导致较低的局部绝热火焰温度,从而减少氮氧化物排放。试验结果表明,烟气与燃料的质量比对NOX减排性能的影响很大。烟气/燃料的夹带质量比通常在每磅燃料2至3磅烟气之间,导致锅炉燃烧器应用的氮氧化物减少约50%至70%。通过上游和下游FIR管道系统的压降影响烟气夹带性能。本文描述了现有FIR系统不满足初始设计性能的优化。为了提高夹带比,采用了多种工具对FIR系统进行了重新设计和优化。这些工具包括计算流体动力学(CFD)、半经验建模和冷流测试结果。对结果进行了详细的描述和讨论。
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Optimizing the Performance of a Fuel Induced Flue Gas Recirculation (FIR) System for Low Nox Boiler Burner Applications
New burner design technologies are using the momentum of fuel gas injection to entrain flue gas for the purpose of diluting the combustible mixture in order to reduce NOX emissions. Using an eductor, these designs entrain flue gas from above the convection section of a furnace stack and mix with the fuel downstream of the eductor. This diluted fluegas/fuel mixture results in lower local adiabatic flame temperatures providing a reduction in NOX emissions. Test results show that NOX reduction performance is strongly dependent on the mass ratio of flue-gas to fuel. An entrainment mass ratio of flue-gas/fuel typically ranges between 2 to 3 pound flue-gas per pound fuel, leading to a NOX reduction of approximately 50 to 70 % for boiler burner applications. The flue gas entrainment performance is effected by pressure drop through the upstream and downstream FIR piping system. This paper describes optimization of an existing FIR system not meeting initial design performance. To improve the entrainment ratio several tools were used to re-design and optimize the FIR system. These tools included Computational Fluid Dynamics (CFD), semi-empirical modeling and cold flow test results. A detailed description and discussion of the results are presented.
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