How to calculate DPM particle flow rate for a 2D axisymmetric case
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Given the 2D geometry with an axis, how do we calculate the flow rate?
Geometry: Attachment 78565 Inlet : Attachment 78566 Surface injection = inlet (6 mesh grid points) , mass flow rate = 3.6513e-6 kg/sec , density = 1.6228 (kg/m3) , Such that wolume flow rate per grid point ( at inlet ) = 2.25 cm3/sec . While applying the axisymmetric case, how will we be able to calculate net flow rate? Had it been a 3D case, I would have multiplied it with the total number of mesh points on the inlet surface. But how may this be in a 2D axisymmetric case? Thanks |
2D axisymmetric
It does not matter whether it is 2D or 3D. It is always the number of mesh points - face centers in case of 3D, and edge centers in case of 2D.
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total flow rate?
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Another question is how will this map to the real case? As we have the axis boundary condition. Since the experiment is actual 3D, What flow rate should I consider in the experiment? Will it be the same, flow rate= 5*(flow rate of 1 point) Thank you. |
experimental flow rate value?
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given dpm particles (argon gas) density = 1.6228 gm/cm3. mass flow rate = 0.01 kg/sec inlet & geometry = already shown in the previous reply above. ( 30 mm in length with 5 edges in the mesh and axisymmetric condition ) With all this information how will I be able to find the volume flow rate which I will set in my experimental setup? Thank you. |
Volume Flow Rate
Volume flow rate is independent of particles or droplets. It is ratio of mass flow rate and density. So, 0.01 / 1.6228. The density value is correct, but the units you mentioned is wrong. The volume flow rate calculated is for full, circular duct.
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calculations
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Will this be the flow rate I would be required to set in the experimental inlet, which is a circular pipe of diameter 60 mm? Model ( 2D axisymmetric ) = Attachment 78589 Experimental setup = Attachment 78590 May you please have a look at the above pictures for reference. Thank you for all the help. |
Volume Flow Rate
Where does 1000 come from? Is it the density of the continuous phase?
Do note that axisymmetric model is valid only for the central inlet. |
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