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Emptying Time of a Tank Filled up with Explosive Paste. Comparison between Experimental Measurements and Predictions Based on Rheological Characterization of the Paste

机译:排空坦克的时间填满了与爆炸的浆糊。基于浆料流变特征的实验测量与预测的比较

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One industrial process used by Nexter Munitions to manufacture pyrotechnical materials consists in preparing an emulsion of wax in TNT (2,4,6-trinitrotoluene) and adding Aluminium and ONTA (3-nitro-1,2,4-triazole-5-one) particles. When the suspension is homogeneous, it is allowed to flow by gravity through a pipe located at the bottom of the tank and to fill up a shell body. The suspension is characterized by a solid volume fraction of 53.4%, which leads to high viscosities. In some circumstances, the emptying time is prohibitively long and the economic profitability is reduced. This study has been performed to make the emptying time lower with the constraint of unchanged volume fractions and grains mean diameter. So, we investigated the influence of the grain size distribution on the suspension viscosity. Different samples of Aluminium and ONTA have been used, with rather small differences in grain size distributions. The suspensions have been prepared in the industrial tank and the flow cast times measured. It has been observed that they differ by one order of magnitude. To avoid situations with too high emptying times, a procedure has been implemented to make prior characterization of the suspension rheology. Because of particles sedimentation and emulsion destabilisation, the classical Couette rheometer is not adapted. So, we designed and built a small size tank (113 cm3), where the suspension is continuously stirred and kept homogeneous. The measurement of the torque and rotational speed together with the use of the Couette analogy allowed us to observe an Ostwald fluid behaviour (flow consistency index k, flow behaviour index n). For a better prediction, we established a correlation between the measured (k, n) values and the grain size distributions. We characterized each suspension by the ratio of to m, where is the solid volume fraction (imposed by the commercial specifications) and m is the maximum packing fraction. Because of the strong analogy between concrete and energetic paste, we chose the widely used De Larrard model to compute m. A linear dependence between the ratio/and the indices k and n was observed. The second step was to provide an analytical expression for the flow cast time of a power-law suspension from a tank with given geometry. Considering the large difference between the industrial inner tank diameter and the evacuation pipe diameter, we assumed that all the pressure drop was located in the evacuation pipe. Then, extending the Hagen-Poiseuille equation to Ostwald fluid, we were able to predict the emptying time with the knowledge of kand n. Experimental and predicted emptying time are in very good agreement. This work helped the industrial manufacturer to divide the emptying time by a factor 12.
机译:Nexter Maritions用于制造烟火材料的一个工业过程包括在TNT(2,4,6-三硝基甲苯甲丁橡胶)中制备蜡的乳液,并加入铝和ONTA(3-硝基-1,2,4-三唑-5-one ) 粒子。当悬浮液是均匀的时,它可以通过位于罐底部的管道流动,并填充壳体。悬浮液的特征在于固体体积分数为53.4%,这导致高粘度。在某些情况下,排空时间非常长,经济盈利能力降低。已经进行了该研究以使排空时间与不变的体积分数和晶粒直径的约束降低。因此,我们研究了晶粒尺寸分布对悬浮粘度的影响。已经使用了不同的铝和ONTA样品,具有相当小的晶粒尺寸分布的差异。悬浮液已经在工业罐中制备和测量的流量铸造时间。已经观察到它们的级别不同。为了避免清空时间过高的情况,已经实施了一种程序以使悬浮流变学的先前表征。由于颗粒沉降和乳液不稳定,古典Coute耦仪不适应。因此,我们设计并制造了一个小尺寸的罐(113cm3),其中悬浮液连续搅拌并保持均匀。扭矩和旋转速度的测量与使用Coute Complyy一起允许我们观察OSTWALD流体行为(流量稠度指数K,流动行为指数N)。为了更好的预测,我们建立了测量(K,N)值与晶粒尺寸分布之间的相关性。我们将每种悬浮液表征为m的比例,其中固体体积分数(商业规格施加),M是最大包装级分。由于混凝土和精力充沛的粘贴之间的强烈类比,我们选择广泛使用的de larrard模型来计算m。观察到比率/和索引K和N之间的线性依赖性。第二步是为来自给定几何形状的罐的动力法悬浮液的流量铸造时间提供分析表达。考虑到工业内罐直径和抽空管直径之间的巨大差异,假设所有压降都位于抽空管中。然后,将Hagen-Poiseuille方程扩展到Ostwald流体,我们能够通过Kand N的知识预测排空时间。实验和预测的排空时间非常良好。这项工作有助于工业制造商将排空时间分为一个因素12。

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