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Numerical Simulation and Experimental Investigation of steam separators

机译:蒸汽分离器的数值模拟与实验研究

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Based on computational fluid dynamics method of two-phase flow,Separation efficiency of steam separator used for steam-water separating in power plant is presented.A mathematical model is established for simulating the flow field of gas flow channels in steam separator.The trajectory of droplets is obtained by using particle motion equation.The gas-water separating efficiency is calculated for the droplets at different particle diameter.The equations are solved by using computational fluid dynamics method.An experimental model is established for determining the structure parameters and critical velocity of steam separator.The results show that structure parameters and inlet gas velocity have great influence on the separation efficiency of wave type plate separator.The separation efficiency of steam separator with hooks is higher than that without it.Plate spacing and length offer the largest opportunity to the performance improvement. The droplets removal efficiency increases with the plate spacing reduction.The turning angle must be less than 54°for a high efficiency and low pressure loss.The gas velocity within the separator should be kept below a critical velocity as well in order to avoid re-entrainment. Numerical and experimctntal results can be directly used for the design of steam separator.
机译:基于两相流计算流体动力学方法,提出了用于电厂汽水分离的蒸汽分离器的分离效率,建立了数学模型来模拟蒸汽分离器中气体流道的流场。通过粒子运动方程得到液滴,计算不同粒径的液滴的气水分离效率,通过计算流体力学方法求解方程,建立确定模型结构参数和临界速度的实验模型结果表明,结构参数和进气速度对波浪型板式分离器的分离效率有很大的影响,带钩的蒸汽分离器的分离效率高于不带钩的分离器,板间距和长度为最大的分离机会提供了条件。性能提升。液滴的去除效率随着板间距的减小而增加。为了获得高效率和低压力损失,转向角必须小于54°。分离器内的气体速度也应保持在临界速度以下,以免再次分离。夹带。数值和实验结果可直接用于蒸汽分离器的设计。

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