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Characterization and modeling of deposition geometry in directed energy deposition over inclined surfaces

机译:倾斜表面定向能量沉积中沉积几何形状的表征与建模

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Directed Energy Deposition (DED) is setting a relatively new trend for the repair and restoration of high value components. Repair of these components necessitates contoured depositions due to the complexity in the geometry. This further demands depositions at various inclination angles. The influence of inclination angle needs to be studied so as to predict the final deposition geometry which will be a function of the powder loss and the melt-flow. Therefore, this study is aimed at exploring the effect of inclination angle on the powder catchment efficiency and shape evolution of the deposited track. Asymmetry is observed in the cross-section of the deposited track while carrying out the DED at an inclination. A two-dimensional transient heat transfer model with fluid flow has been developed to predict the temperature distribution, track melt pool boundary during the deposition process. The solidification and the arrest of the melt pool flow is accounted by employing the enthalpy porosity model. The model is used to predict the deposition geometry. Predicted deposition geometry values agree reasonably well with the experimental results. This model is used to recognize the factors contributing towards this asymmetry during the deposition at inclination. The study reveals that there is a substantial drop in the powder catchment efficiency from 66% to 19% as the inclination angle is increased from 0o to 75o. In order to have uniform clad, increasing mass flow rate is a viable option as the catchment efficiency is almost unchanged with increasing mass flow rate.
机译:定向能源沉积(DED)正在为高价值组件的修复和恢复设定相对较新的趋势。这些组件的修复需要由于几何形状的复杂性而导致的轮廓沉积。这进一步要求以各种倾斜角度沉积。需要研究倾斜角度的影响,以预测最终的沉积几何形状,这将是粉末损耗和熔体流动的函数。因此,本研究旨在探讨倾斜角度对沉积轨道的粉末集水效率和形状演化的影响。在沉积的轨道的横截面中观察到不对称,同时在倾斜度下进行DED。已经开发出具有流体流动的二维瞬态传热模型来预测沉积过程中的温度分布,跟踪熔池池边界。通过使用焓孔隙度模型来沉默凝固和熔体池流动。该模型用于预测沉积几何形状。预测的沉积几何值与实验结果相加。该模型用于识别在倾斜沉积期间有助于这种不对称的因素。该研究表明,随着倾斜角度从0O至75O增加,粉末集水区效率从66%到19%的大幅下降。为了具有均匀的包层,随着量散流速的增加几乎不变,增加质量流量是可行的选择。

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