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Issues with an attempt to model an inline tube bank |
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October 12, 2011, 08:01 |
Issues with an attempt to model an inline tube bank
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New Member
Andrew Muharib
Join Date: Aug 2011
Posts: 3
Rep Power: 14 |
Hi all I am very new to using STAR CCM+ and was wondering if some one could help me with my dilemma. I have both a Hi and Low Re meshes designed to model flow through a 2x2 inline tube bank. I am modelling the turbulent flow through the 3-D system by including periodic boundaries on x, y and z directions. Essentially trying to observe the pressure, coefficient of pressure, and nusselt number around the central tube. The model description is presented below:
Model Considered - Constant Density Gas - Air High y+ wall treatment Implicit Unsteady RANS Reynolds Stress Model Quadratic Pressure Strain (which is the same as SSG) Segregated Flow and Fluid Temperature Three Dimensional Turbulent Air properties: Density = 1.0 Dynamic viscosity = 2.43902439 x10-5 (1/Reynolds number) and Re = 41,000 Specific heat = 1009 Thermal conductivity = 0.0024609756 (viscosity x specific heat) Turbulent Prandtl Number = 1.0 Initial conditions: Pressure = 0.0 Static temperature = 500K Turbulence intensity = 0.03 Turbulent velocity scale = 1.0 Turbulent Viscosity ratio = 10 Velocity = 1.0 Reference Values: Min allowable wall distance = 1.0 x 10-6 Min allowable temp = -500 k ( I know this is completely unrealistic however I am using temperature as a passive scalar so it really has no knock on effect to the density and rest of the calculation) Max allowable temp = 5000k Reference Pressure = 0.0 I am struggling with a few problems: 1) Defining the correct stopping criteria and time step for the implicit unsteady solver. 2) I have managed to simulate pressure differences with the simulations I have run so far, however I cannot seem to get the nusselt number plots to work correctly i.e. I get nothing. 3) I am essentially trying to model an inline tube bank, hence the periodic boundaries. I have set the y and z - periodic boundaries with a zero pressure jump. Yet the x - direction periodic boundary has been defined with a mass flow rate of 0.12 kg/s in order to drive the flow. I was wondering if this approach was correct. Any help would be greatly appreciated. Thank you. |
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