Improving Efficiency of Steam Separators in Power Plant

Lichun Xiao, Zhijiang Ding, Qiang Li, Jing-fei Yang
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引用次数: 4

Abstract

In order to separate droplets from the steam, a new type steam separator with high efficiency in power plant is presented. An experimental model is established for determining the structure parameters and critical velocity of steam separator. Fibreglass filtering method is used for measuring the Separation efficiency of steam separator. The results show that separation efficiency of the steam separator with collecting hooks is higher than that of without it. The plate length of the steam separator has almost no effect on the separation efficiency. The turning angle of the separator is at 54º, the plate spacing is at 20 mm and the critical velocity is at 5 m/s to improve the efficiency. The water film adhering on the plate wall will break when the gas velocity is more than the critical velocity. The separation efficiency decreases and secondary liquid entrainment increases significantly. Separation efficiency of steam separator is high when moisture content of inlet gas is less than 30 g/m3, however, it is low when moisture content of that is more than 50 g/m3. The optimum structure parameters and empirical formula of separation efficiency can be obtained from the experimental analysis. It is beneficial to the industrial design of steam separator in power plant.
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提高电厂蒸汽分离器效率
为了分离蒸汽中的液滴,提出了一种新型高效蒸汽分离器。为确定蒸汽分离器的结构参数和临界速度,建立了实验模型。采用玻璃纤维过滤法测定蒸汽分离器的分离效率。结果表明,带收集钩的蒸汽分离器的分离效率高于不带收集钩的蒸汽分离器。蒸汽分离器的板长对分离效率几乎没有影响。分离器的转角为54º,板间距为20 mm,临界速度为5 m/s,以提高效率。当气速大于临界速度时,附着在板壁上的水膜就会破裂。分离效率降低,二次携液量明显增加。当入口气体含水率小于30 g/m3时,蒸汽分离器的分离效率较高,当入口气体含水率大于50 g/m3时,分离效率较低。通过实验分析,得到了最佳结构参数和分离效率的经验公式。对电厂汽分离器的工业设计有一定的参考价值。
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