首页> 外文会议>International topical meeting on advances in thermal hydraulics;American Nuclear Society meeting >EFFECT OF GLASS VISCOSITY ON FOAMING BEHAVIOR AND HEAT TRANSFER IN A LABORATORY-SCALE WASTE GLASS MELTER
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EFFECT OF GLASS VISCOSITY ON FOAMING BEHAVIOR AND HEAT TRANSFER IN A LABORATORY-SCALE WASTE GLASS MELTER

机译:玻璃粘度对实验室级废玻璃熔窑起泡行为和传热的影响

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A computational fluid dynamics model was developed to support the testing of a laboratory-scale waste glass melter. This work focuses on providing an understanding of how the heat flux convected from the melt pool is affected by the forced bubbling and by the foam layer underneath the cold cap formed by reaction gases. Simulations were performed for high-level waste glass simulants with viscosities near the minimum and maximum values that are expected during the Hanford tank waste vitrification campaign. The model resolves the forced convection bubbling in the molten glass and bubbles in the foam that forms beneath the cold cap. The glass with higher viscosity shows the formation of significantly larger bubbles to overcome the higher viscous force. The foaming thickness under the cold cap in higher viscosity cases is cleared less easily than the low viscosity glass case. However, the percentage of foam in contact with the cold cap is decreased at higher viscosity since the higher viscous force tends to prevent direct contact. This trend is reversed when there is no forced convection supplied by the bubblers. The heat fluxes at the bottom of the cold cap are compared for cases with and without forced convection bubbling. As expected, the convective heat flux increases with bubbling, and the average values for heat transfer coefficients from the CFD show reasonable agreement with Nusselt number correlations for flat plates.
机译:开发了计算流体动力学模型来支持实验室规模的废玻璃熔融器的测试。这项工作的重点是提供对从熔池对流的热通量如何受到强制鼓泡以及反应气体所形成的冷盖下方的泡沫层的影响的理解。对高粘度废玻璃模拟物进行了模拟,其粘度接近汉福德罐废玻璃化运动中预期的最小和最大值。该模型解决了熔融玻璃中的强制对流冒泡以及冷盖下方形成的泡沫中的气泡。具有较高粘度的玻璃显示出明显更大的气泡,以克服较高的粘性力。与低粘度玻璃箱相比,高粘度箱中的冷盖下的泡沫厚度难以清除。然而,由于较高的粘性力倾向于防止直接接触,因此在较高的粘度下与冷盖接触的泡沫的百分比降低。当起泡器没有提供强制对流时,这种趋势将逆转。比较有无强制对流鼓泡情况下冷帽底部的热通量。正如预期的那样,对流热通量会随着鼓泡而增加,并且CFD的传热系数平均值与平板的Nusselt数相关性显示出合理的一致性。

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