Mathematical modeling of gas dynamics and off-gas post-combustion above the melt in a melter-gasifier furnace

T. V. Erokhov, I. A. Levitskii, G. S. Podgorodetskii, V. Gorbunov
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Abstract

Organization of technological process and design of a furnace significantly affect the parameters of post-combustion, determining the need to develop a mathematical model of post-combustion zone. Modeling of gas dynamics, chemical reactions, convective diffusion and heat transfer in the gas phase above the melt was carried out in an experimental melter-gasifier furnace at three different values of mass flow rates and two positions of post-combustion tuyeres. Temperature distributions and off-gas components concentrations were obtained. It was found that at the lower position of the tuyere, post-combustion is carried out in the area of reflected jet, stagnant zones are formed around the tuyere and between the reflected jet and the melt surface, which decrease the post-combustion level. At the upper position of the tuyere, post-combustion occurs inside the primary jet, intensive mixing of all components of the furnace atmosphere occurs, post-combustion undergoes more completely, which leads to an increase in the off-gases temperature with an increase in uniformity of temperature fields and concentrations compared with the lower position of the tuyere. At the lower position of the tuyere, the flame zone turns out to be open, its shape significantly depends on the mass flow, and the flame zone volume increases with an increase in the mass flow. At the upper position of the tuyere, the flame zone is closed, with an increase in the mass flow, its shape does not change, but the flame zone volume decreases. For reduction processes in slag melt, the upper position of the tuyere is preferable, while for production of the producer gas at the furnace outlet, position of the tuyere closer to the melt surface is preferable.
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熔化炉-气化炉中熔体上方气体动力学和废气后燃烧的数学建模
技术工艺的组织和熔炉的设计对燃烧后的参数有很大影响,因此需要建立燃烧后区域的数学模型。在一个实验性熔化炉-气化炉中,在三种不同的质量流量值和两个后燃烧簇位置下,对熔体上方气相中的气体动力学、化学反应、对流扩散和传热进行了建模。获得了温度分布和废气成分浓度。结果发现,在风口位置较低时,后燃烧在反射射流区域进行,风口周围和反射射流与熔体表面之间形成停滞区,从而降低了后燃烧水平。在风口的上部位置,后燃烧发生在主射流内部,炉内气氛的所有成分发生强烈混合,后燃烧进行得更彻底,这导致废气温度升高,与风口的下部位置相比,温度场和浓度的均匀性提高。在风口的较低位置,火焰区是开放的,其形状主要取决于质量流量,火焰区的体积随着质量流量的增加而增大。在推流器的上部位置,火焰区是封闭的,随着质量流量的增加,火焰区的形状不会改变,但火焰区的体积会减小。对于炉渣熔体的还原过程来说,最好将风口设置在上部位置,而对于在熔炉出口处生产煤气来说,最好将风口设置在靠近熔体表面的位置。
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