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基于F曲線的中間包流場優化

Optimization of the tundish flow field based on F-curve

  • 摘要: 針對某廠三流異型坯中間包,建立了相似比為1∶2的水模型,使用F曲線對不同控流裝置下的中間包流場特性進行分析與優化。實驗內容包括原型控流裝置、湍流抑制器無擋壩、湍流抑制器加擋壩組合。結果表明,原型中間包中部水口存在短路流,水口間流動的差異性較大,可能導致三個鑄流的鑄坯溫度和潔凈度不均勻,進而發生同爐次各鑄坯質量穩定性差的問題。采用湍流抑制器無擋壩控流裝置,湍流抑制器導流孔夾角為60°時,短路流出現在中部;導流孔夾角為86°時,無短路流,各流一致性變好;導流孔夾角為110°時,兩側水口出現短路流,各流一致性優于前兩個角度。中間包的各流一致性與死區比例并無相關性,一致性良好的中間包流場,其死區比例并不一定小。優化后的中間包湍流抑制器導流孔夾角為110°,擋壩距離中間包中心2400 mm,中間包內無短路流,1#、2#水口一致性最佳,死區由17.89 %減小到9.67 %,減小率為11.25 %,F曲線標準差最大值由0.3減小到0.016。

     

    Abstract: The water model with a similarity ratio of 1∶2 was established for a three-strand beam blank tundish. The molten steel flowing character was researched in different flow control devices by using the F-curve, and the flow field of the tundish was optimized. The volume fractions of dead region, plug flow and well-mixed flow are calculated. The standard deviation of the stagnation time of 1, 2 and 3 flow and the maximum value of standard deviation function of F-curve were used to evaluate the dispersion of each flow. Three cases were considered during the experiments, i.e, prototype flow control device, turbulence inhibitor without dams combination, turbulence inhibitor and dams combination. The results show that short circuit flow exists in the middle nozzle of the prototype tundish, and poor consistency between nozzles, which may lead to the uneven temperature and cleanness of the three-strand beam blanks, leading to different quality of different beam blanks in one heat. Using the turbulence inhibitor without dams combination, the short circuit flow appears in the middle of tundish with the angle of diversion holes being 60°. When the angle is 86°, there is no short circuit flow, and the consistency between strands becomes better. When the angle is 110°, the short circuit flow appears in the two sides of the tundish nozzle with the best consistency between strands. There is no correlation between the consistency of the tundish strands and the dead volume fraction. When the consistency of the tundish strands is good, the dead volume fraction may not be small. After optimization, the angle of the diversion hole of the tundish turbulence inhibitor is 110°, the dam is 2400 mm away from the tundish center. There is no short-circuit flow, the consistency of 1# and 2# nozzles is the best, the dead volume fraction is reduced to 9.67% from 17.89%, and the reduction rate is 11.25%. The maximum standard deviation of the F-curve is reduced to 0.016 from 0.3.

     

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