本案例演示高Weissenberg数下粘弹性流体流动计算。流体介质粘度采用Phan Thien-Tanner粘弹性模型,其参数为:
1 案例描述
案例轴对称几何模型如下图所示。尺寸x=[0, 4], y = [-20, 20]。入口及出口体积流量Q=3.1415926。
2 Polyflow设置
2.1 读取网格
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如下图所示导入计算网格contr41.msh
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双击单元格Setup进入Polydata
2.2 创建Task
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Create Task
:F.E.M. task, Evolution, 2D axisymmetric geometry
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Create a subtask
: Differential viscoelastic isothermal flow problem
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Domain
: Subdomain 1
2.3 定义材料
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选择Differential viscoelastic models
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选择1-st viscoelastic model
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选择Phan Thien-Tanner model
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设置材料参数visc = 1.0;trelax = 5.0,EVOL: f(S) = S;eps = 0.015;xi = 0.2;ratio = 0.11112
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No density
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no inertia
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no gravity
2.4 边界条件指定
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BS1: Inflow; flow rate = 3.141593 (fully developed, volumetric)
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BS2: vn = vs = 0
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BS3: Outflow; flow rate = 3.141593 (fully developed, volumetric)
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BS4: axis of symmetry
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Interpolation:
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Coordinates
: linear -
Stresses
: 4x4 SU for element -
Velocities
: quadratic -
Pressure
: linear
2.5 指定压力与流函数
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进入F.E.M Task 1面板,如下图所示
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Assign the pressure:
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p=0,坐标(0, 20)
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Assign the stream function:
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ψ = 0 ,坐标 (4, -20)
2.6 指定数值参数
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Evolution parameters:
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Initial value of S = 0
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Upper limit of S = 1
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Initial value of delta-S = 0.01
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Min. admissible value of delta-S = 0.0001
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Max. admissible value of delta-S = 0.25
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Max. number of successful steps = 20
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Implicit Euler method for the integration
2.7 Output
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Default output : CFD-Post
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System of units for CFD-Post: metric_mm/ g/ s/ A+Celsius
3 计算结果
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速度分布
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