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FLOW CHARACTERISTICS OF CONTRA- AND CO-ROTATING SWIRLER ARRANGEMENTS OF AN INDUSTRIAL COMBUSTOR

机译:工业燃烧室对流和同向旋转旋流器布置的流动特性

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This paper describes the investigation of the flow characteristics of two double radial inflow swirlers configured for use in a gas turbine combustor. The only difference between the two swirlers is in the contra- and co-rotating flow of air in the inner nozzle arrangement. The isothermal vortex flow field created by the double swirlers has been examined using numerical Model 1. The model also includes a cylinder reaction zone downstream of the swirler. The comparison of flow characteristics is carried out by examination of the spatial resolution of three mean velocity components. The contra- and co-rotating configurations show some discrepancy in terms of total loss factor and mass split ratio between the two swirlers. The comparison of flow fields also indicate that there is almost no remaining swirl further downstream in the contra-rotating configuration, while a significant amount of remaining swirl exists for the co-rotating option. The development of Model 1 to include a typical dilution zone and transition duct leads to numerical Model 2, which was used to investigate the impact on downstream mixing with the dilution air and the emerging temperature distribution at the transition duct exit. Comparing the temperature field for both configurations, the dilution effectiveness increases significantly with dilution jet penetration depth and reduces with spread along the circumferential direction. These effects lead to the central hot core persisting along the transition duct to the combustor outlet for the co-rotating option due to the combination of initial cross flow and a strong swirl, resulting in a considerable difference in the predicted outlet temperature distribution factors (OTDF) of 10.8% and 17.7% for the contra- and co-rotating arrangements, respectively.
机译:本文介绍了对配置用于燃气轮机燃烧室的两个双径向入流旋流器的流动特性的研究。两个旋流器之间的唯一区别在于内部喷嘴装置中空气的对流和同向旋转。使用数值模型1检查了由双旋流器产生的等温涡旋流场。该模型还包括旋流器下游的圆柱反应区。流动特性的比较是通过检查三个平均速度分量的空间分辨率来进行的。对流和同向旋转配置在两个旋流器之间的总损耗因子和质量分配比方面显示出一些差异。流场的比较还表明,在反向旋转配置中,在更下游的位置几乎没有残留涡流,而对于同向旋转选项则存在大量的残留涡流。模型1的开发包括一个典型的稀释区和过渡管道,导致了数值模型2的产生,该模型用于研究稀释空气对下游混合的影响以及过渡管道出口处出现的温度分布。比较两种配置的温度场,稀释效率随着稀释射流穿透深度的增加而显着增加,并随着沿周向方向的扩散而降低。由于初始横流和强烈涡流的结合,这些效应导致中央热芯沿着过渡管道一直沿燃烧室出口进行同向旋转,这导致了预计出口温度分布系数(OTDF)的显着差异)(分别为对向旋转和同向旋转),分别为10.8%和17.7%。

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