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NO_x Formation and Reduction With NH_3 in Fluidized Bed Combustion - The Influence of the O_2 Concentration on the Kinetics

机译:NH_3在流化床燃烧中形成和减少NH_3 - O_2浓度对动力学的影响

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In (circulating) fluidized bed combustors, NO_x and N_2O emissions originate mainly from nitrogen in the fuel. The formation of NO_x and reduction to N_2 follow complicated reaction paths involving both homogeneous and heterogeneous reactions. In these reaction paths oxygen plays an important role. When air staging is used in a (circulating) fluidized bed combustor, the O_2 concentration in the combustor varies over a broad range. Limestone, used as a sorbent for sulfur retention, is a good catalyst for the formation of NO_x. In this study the influence of the O_2 concentration is investigated on homogenous reactions and on reactions catalysed by limestone. In a fixed bed reactor the NO formation and reduction reactions are studied at 850°C. With a kinetic model, rate expressions for the NO formation and reduction reactions are obtained from experimental data. The results show, that the O_2 concentration has an influence on the homogenous formation and reduction of NO, which differs from most literature that assumes a zero dependency. For the reactions catalysed by CaO, no influence of the O_2 concentration was found. Rate expressions for the homogeneous reduction and oxidation reactions that are O_2 dependent, give a good description of the O_2 influence on the homogenous NO formation and reduction. The rate of the reduction reaction was similar to the one reported by Jensen et al. (1995). The rate of the oxidation reaction is found to be 50 percent lower. For the heterogenous oxidations, O_2 independent rate expressions are obtained that give a reasonably good description of the NO formation. The O_2 dependency found in the heterogenous experiments is caused by the homogeneous reactions that are O_2 dependent. The rate constants of the heterogenous reaction found in this work are significantly higher than the ones found by Johnsson (1990). With the model developed in this work, it is possible t o predict the influence of O_2 concentration on the emissions of NO and NH_3.
机译:在(循环)流化床燃烧室中,NO_X和N_2O排放主要来自燃料中的氮。 NO_X的形成和降低到N_2遵循涉及均相和异质反应的复杂反应路径。在这些反应路径中,氧气起着重要作用。当在(循环)流化床燃烧器中使用空气分段时,燃烧器中的O_2浓度在宽范围内变化。石灰石,用作硫潴留的吸附剂,是用于形成NO_X的良好催化剂。在这项研究中,研究了O_2浓度的影响在均匀反应和石灰石催化的反应上。在固定床反应器中,在850℃下,没有形成没有形成和还原反应。通过动力学模型,无形成和还原反应的速率表达是从实验数据中获得的。结果表明,O_2浓度对均匀形成和否的影响产生影响,这与归零依赖性的大多数文献不同。对于CaO催化的反应,未发现O_2浓度的影响。均匀降低和氧化反应的速率表达是O_2所依赖的,良好描述对O_2对均匀的不形成和还原的影响。还原反应的速率类似于Jensen等人报告的速率。 (1995)。氧化反应的速率被发现为50%。对于异源氧化,获得O_2的独立速率表达,其给出了无形成的合理描述。在异构实验中发现的O_2依赖性是由均匀的均相反应引起的。本工作中发现的异源反应的速率常数显着高于约翰逊(1990)所发现的反应。通过在这项工作中开发的模型,可以预测O_2浓度对NO和NH_3排放的影响。

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