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Numerical comparison on the influence of geometric size on melt viscosity for conventional and gas-assisted extrusion of plastic micro-tube

机译:几何尺寸对常规和气体辅助挤出熔体粘度影响的数值比较

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We studied the effects of the geometric size on the viscosity of melt for plastic micro-tubes with different radius or L/D ratios by using the finite element method in this paper. Meanwhile, the Bird-Carreau constitutive model was used to describe the rheological properties of non-Newtonian melt. Two of geometric models were used in this study. For the geometric model with same L/D ratio but different radius, the same inlet pressure value was imposed on the inlet face of geometric model. For the geometric model with the same radius but different L/D ratios, the same inlet volume flow rate of melt were imposed on the inlet face of geometric model. Numerical results show that, for the conventional extrusion of plastic micro-tubes with same L/D ratio but different radius, the apparent viscosity of melt decreases with the decreasing of the radius. For the plastic micro-tubes with same radius but different L/D ratios, the apparent viscosity of melt is nearly not changed with the decreasing of the L/D ratio. However, for the gas-assisted extrusion of plastic micro-tube, the geometric size doesn't seem to affect the melt viscosity.
机译:我们通过在本文中使用有限元方法研究了几何尺寸对塑料微管熔体粘度的影响,通过使用本文的有限元方法,使用不同的半径或L / D比。同时,鸟库本构模型用于描述非牛顿熔体的流变性质。本研究使用了两种几何模型。对于具有相同L / D比但半径不同的几何模型,对几何模型的入口面积施加相同的入口压力值。对于具有相同半径但不同的L / D比的几何模型,对几何模型的入口面施加相同的入口体积流量。计算结果表明,对于塑料微管具有相同的L / d比,但不同半径的常规挤出,熔体的表观粘度随半径的减小而减小。对于具有相同半径但不同的L / D比的塑料微管,熔体的表观粘度几乎没有随着L / D比的降低而改变。然而,对于塑料微管的气体辅助挤出,几何尺寸似乎似乎不会影响熔体粘度。

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