首页> 外文会议>The Belton Memorial Symposium Proceedings, Jan 10-11, 2000, Sydney, Australia >Some Observations on the Draining of CaO-SiO_2-Al_2O_3 Slag Bubble Films
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Some Observations on the Draining of CaO-SiO_2-Al_2O_3 Slag Bubble Films

机译:CaO-SiO_2-Al_2O_3矿渣气泡膜排水的一些观察

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1. No clear relationship between the draining rate and melt viscosity could be established, as viscosity could not be independently changed without decreasing the slag surface tension. Although the film draining rate increased with increasing temperature, a complicated trend was observed for the draining of CaO-SiO_2-Al2O_3 films as a function of SiO_2 concentration. The addition of up to 10 wt % Fe_2O_3 to the slags was expected to increase the film draining rate, if bulk viscosity were to strongly influence their draining behaviour. However, iron-oxide additions were found to dramatically decrease the draining rate of the films, irrespective of temperature. Clearly, further work is required to explain any likely influence of slag viscosity on the draining rate of bubble films. 2. Drainage of the liquid within the film 'Plateau borders' themselves showed a very strong temperature dependence, ie., the calculated activation energy for border thinning (~ 150 kJ/mol) was very close to that calculated for viscous flow within the slag system studied (~ 160 kJ/mol). This suggests that, as within aqueous foam films, bulk viscosity of the continuous phase can play an important role in foam drainage, once the liquid reaches the Plateau borders under capillarity. Surface tension was shown to exert a very strong influence on the draining rate of CaO-SiO_2-Al_2O_3 slag bubble films. Addition of dilute concentrations of strong surface-active agents (such as P_2O_5 and Na_2O) to lower the surface tension of the slags, resulted in a profound decrease in their draining rate, irrespective of temperature. The above results suggest the physics of liquid film drainage within silicate slag films and Plateau borders to be similar to those encountered in typical aqueous systems. 3. A crude correlation has shown that the rate of draining of liquid within CaO-SiO_2-Al_2O_3 slag bubble films at 1673 K is strongly influenced by the (estimated) rate of surface tension lowering, per unit concentration change of surfactant (dγ/dC). That is, the higher the estimated value of dγ/dC for a given surface-active agent, the higher the resulting "retardatory index," ie., the greater the magnitude of the decrease in film draining rate after surfactant addition. Limited results obtained by the authors for an independent Na_2O-B_2O_3 'model' system at 1233 K also agreed with this trend. Further data treatment is necessary in order to quantify the true physical meaning of the proposed "retardatory index." 4. The slag bubble films in this study appear to show thinning characteristics similar to those observed in aqueous bubble films, ie., at the well-drained stages, the films tend to become uniform in thickness, prior to rupture at thicknesses of δ ~ 0.1 - 0.2 μm.
机译:1.由于无法在不降低炉渣表面张力的情况下独立改变粘度,因此无法确定排水速率与熔融粘度之间的明确关系。尽管随着温度的升高,薄膜的排水速率增加,但观察到复杂的CaO-SiO_2-Al2O_3薄膜的排水趋势是SiO_2浓度的函数。如果堆积粘度强烈影响其排泄性能,则期望向渣中添加至多10 wt%的Fe_2O_3可以提高薄膜的排泄速率。然而,发现氧化铁的添加显着降低了膜的排水速率,而与温度无关。显然,需要进一步的工作来解释炉渣粘度对气泡膜排放速率的任何可能影响。 2.薄膜“高原边界”本身内的液体排放显示出非常强的温度依赖性,即,计算出的边界变薄活化能(〜150 kJ / mol)非常接近于炉渣中的粘性流所计算出的活化能。系统研究(〜160 kJ / mol)。这表明,如同在水性泡沫膜中一样,一旦液体在毛细管作用下到达高原边界,连续相的体积粘度就可以在泡沫排水中发挥重要作用。结果表明,表面张力对CaO-SiO_2-Al_2O_3渣泡膜的排水速率有非常大的影响。添加稀浓度的强表面活性剂(例如P_2O_5和Na_2O)以降低炉渣的表面张力,从而导致其排泄速率大大降低,而与温度无关。以上结果表明,硅酸盐矿渣膜和高原边界内的液膜排水的物理过程与典型水系统中遇到的情况相似。 3.粗略的相关性表明,CaO-SiO_2-Al_2O_3矿渣气泡膜在1673 K时的排液速率受表面张力降低的(估计)速率(表面活性剂每单位浓度变化(dγ/ dC)的强烈影响) )。即,对于给定的表面活性剂,dγ/ dC的估计值越高,所得的“延迟指数”越高,即,在添加表面活性剂之后膜排水速率降低的幅度越大。作者在1233 K上对独立的Na_2O-B_2O_3'模型'系统获得的有限结果也同意这一趋势。为了量化提议的“延​​迟指数”的真实物理意义,有必要进行进一步的数据处理。 4.本研究中的渣泡膜似乎表现出与水泡膜相似的减薄特性,即在排水良好的阶段,膜在达到δ〜破裂厚度之前趋于均匀。 0.1-0.2微米

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