Distribution characteristic and formation process of bubbles in foaming slag in a converter
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摘要: 在轉爐留渣-雙渣工藝脫磷階段結束倒渣時,分別使用樣勺獲取倒渣開始時上部泡沫渣,倒渣結束時下部泡沫渣以及倒渣結束后爐內剩余底部泡沫渣,使用宏觀及微觀的方法分別分析泡沫渣各部位氣泡分布特點.結果表明:氣泡平均當量直徑,上部>下部>底部;孔隙率,上部>下部>底部.轉爐泡沫渣的形成過程為:隨著大量CO/CO2氣泡進入渣中,氣泡之間不斷碰撞、合并,上部氣泡被下部氣泡抬擠且由于氣泡本身的浮力作用,氣泡不斷上升,氣泡在上升時由于重力作用,氣泡之間渣相在重力作用下析液,氣泡的拓撲結構不斷發生變化,同時氣泡之間不斷碰撞、合并,最后形成上部氣泡直徑大且孔隙率高,下部氣泡直徑小且孔隙率低的泡沫渣.Abstract: Foaming slags at the top at the beginning of deslaggging, in the lower portion at the end of deslagging, and at the bottom after deslagging were taken with a sample scoop at the end of dephosphorization in the converter slag-remaining and double-slag process. The distribution characteristic of bubbles was analyzed by the macro & micro analysis technique. The results indicate that the order of average equivalent diameter of bubbles is the slag at the top > slag in the lower > slag at the bottom, and the order of gas porosity is the slag at the top > slag in the lower > slag at the bottom. The formation process of foaming slags was observed and analyzed. Bubbles collide and coalesce with CO/CO2 moving into the slag. Bubbles in the upper are elevated by bubbles in the lower and the bubbles rises up with buoyancy. The drainage of liquid slag occurs with gravity and the topological structure of bubbles changes. With bubble collision and coalescence, the foaming slag with larger bubbles and higher porosity in the upper and that with smaller bubbles and lower porosity in the lower are formed.
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Key words:
- converters /
- foaming slag /
- bubbles /
- distribution /
- formation mechanisms
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