基于Flow-3D二次氧化渣分布模拟的风电轮毂铸造工艺优化

    Casting Process Optimization of Wind Power Hub Based on Flow-3D Simulation of Secondary Oxidation Slag Distribution

    • 摘要: 风电轮毂铸件严苛的使用环境要求其组织致密、性能优良。在铸造充型过程中形成的二次氧化渣极易造成局部应力集中,严重影响其服役性能。因此预测二次氧化夹渣产生位置并加以控制成为工艺设计的关键。本文完成了风电轮毂铸件的铸造工艺设计,并借助Flow-3D软件模拟了风电轮毂铸件的充型过程,分析了充型速度和内浇口位置对充型平稳度的影响,通过跟踪二次氧化渣的浓度预测二次氧化渣可能形成的部位,提出了工艺优化方案:半封闭底注式浇注系统,横浇道为水平方向的变截面梯形,三个圆形截面内浇口位置正对于弧面大凸台,截面积FFF之比为1 ∶ 2.4 ∶ 1.7,浇注温度1360℃,浇注速度1.3 m/s。采用优化后的工艺方案进行充型过程模拟,发现桨叶孔大平面的拐角处以及铸件下表面的二次氧化渣浓度由500 kg/m3降低到100 kg/m3以下,铸件上表面浓度大于500 kg/m3,大部分的二次氧化渣已转移到铸件上表面,说明优化的铸造工艺方案是合理的,并通过试验件进行了验证。

       

      Abstract: Due to the harsh service environment, wind power hub castings are required to have dense structure and excellent mechanical performance. The secondary oxidation slag formed during the casting filling process is prone to cause local stress concentration, which seriously affects its service performance. Therefore, predicting the location of secondary oxidation slag inclusion and avoiding it has become the key to process design. The casting process design of wind power hub castings was completed and the filling process of wind power hub castings was simulated with the help of Flow-3D software. The influence of filling speed and ingate position on filling stability were analyzed, and the possible formation parts of secondary oxidation slag were predicted by tracking the concentration of secondary oxidation slag, and the process optimization scheme proposed as following: semi-closed bottom gating system, with horizontal variable cross-section trapezoidal runner, three circular cross-section ingates positioned directly opposite the large arc bosses, the cross-sectional area ratio of FingateFrunnerFsprue being 1 ∶ 2.4 ∶ 1.7, pouring temperature of 1360 ℃, and pouring speed of 1.3 m/s. Simulation of the mold filling process using the optimized process scheme reveals that the concentration of secondary oxidation slag at the corners of the large plane of the blade hole and the lower surface of the casting are reduced from 500 kg/m3 to below 100 kg/m3, while the concentration on the upper surface of the casting exceeded 500 kg/m3. Most of the secondary oxidation slag is transferred to the upper surface of the casting. These indicate that the optimized casting process scheme is reasonable, which is verified by experimental specimens.

       

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