Modeling Non-Equilibrium CO Oxidation in Combustion Systems

B. Adams, M. Cremer, David H. Wang
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引用次数: 12

Abstract

Performance of industrial and utility combustion systems is becoming increasingly affected by limits on pollutant emissions such as NOx and CO. CO emissions impact design and operation of combustion systems, particularly when coupled with NOx reduction technologies that involve lower temperature operation or staged firing. Lower combustion temperatures or delayed mixing of fuel and air helps minimize NOx formation, but can increase CO concentrations and minimize CO oxidation rates. Reacting computational fluid dynamics (CFD) models have been shown to be useful in evaluating and optimizing performance of these new technologies and operating conditions. These CFD models have traditionally used equilibrium chemistry models to predict specie concentrations throughout the combustor, however equilibrium assumptions for CO oxidation at lower temperatures is inaccurate. A non-equilibrium CO model is required to accurately predict the oxidation of CO at temperatures lower than ∼1150 K. This paper reviews the development of a non-equilibrium CO model and integration with a reacting CFD model. The use of the resulting model is illustrated on two combustion systems — a waste gas incinerator and a cyclone-fired utility boiler. Results show that low temperature CO oxidation can be accurately predicted with the use of the non-equilibrium CO model.
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模拟燃烧系统中的非平衡CO氧化
工业和公用事业燃烧系统的性能越来越受到氮氧化物和一氧化碳等污染物排放限制的影响。一氧化碳排放影响燃烧系统的设计和运行,特别是当与涉及低温操作或分级燃烧的氮氧化物还原技术相结合时。降低燃烧温度或延迟燃料与空气的混合有助于减少NOx的形成,但会增加CO浓度并降低CO氧化速率。反应计算流体动力学(CFD)模型已被证明在评估和优化这些新技术和操作条件的性能方面非常有用。这些CFD模型传统上使用平衡化学模型来预测整个燃烧室的物质浓度,但是在较低温度下CO氧化的平衡假设是不准确的。需要一个非平衡CO模型来准确预测CO在低于~ 1150 K的温度下的氧化。本文综述了非平衡CO模型的发展及其与反应型CFD模型的结合。结果表明,该模型的使用两个燃烧系统-一个废气焚烧炉和一个旋风燃烧的公用事业锅炉。结果表明,采用非平衡CO模型可以准确地预测CO的低温氧化。
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