I am tring to find the pressure drop as air flows over 1 convulation of louvered fins.
experimentally the pressure drop comes out to be 450Pascals at an inlet velocity of 8m/s
For CFD Simulation, i created an external volume
The inlet side extends to about 1.5 times fin depth and the outlet side extends to 0.8times fin depth.
The boundary conditions applier by me are
Inlet Velocity : 8m/s
Outlet Pressure: 0Pa (gage)
slip/symmetry conditions were applied to two of the sides of the external volume (the one which is almost parallel to the fin plane, i.e. the one having more width)
Now exmaining the result
pressure at inlet of external volume : 210Pa
pressure at outlet of external volume: 0Pa
This is not in agreement with the experimental Data.Could anyone tell where I am going wrong?
I couldnt upload the CFDfile as the system on which cfdesign is installed has no net connection as it contains propriety patented designs
Eagerly looking forward to some response
Dipl.-Ing. (FH) Marco Müller
Application Engineer Digital Simulation
Mensch und Maschine Deutschland GmbH
www.mum.de/cfd
You might try Adv2 and the eddy viscosity turbulence model with a turb/lam ratio of 10. If the solution is is still unstable, try a ratio of 100.
Hope this helps.
Is it possible for you to update to the latest version of SIMCFD (V2015)?
The mesh is not about the number of elements.
When you quote 3M or 12M elements, is this from the Mesh Estimator (on the mesh dialog), or fro the Output Bar / Status file?
If the former, this may not be the actual element count, check the output bar or status file for the actual element count.
Now there are models where 3M is very coarse as it is not about the number of elements but where and how those elements are used.
For your model, through the flow passages what does the mesh look like, how many elements do you have across the gap?
Based off your comment, the pressure you are expecting, how is that lab test configured? Does it allow bypass flow as you mentioned you have in the CFD model? If not, you will need to modify the geometry to prevent this
Well I did refine the mesh further. started having meshing issues so had to fine tune the geometry in CAD then used the edge removal tool in CFDesign to remove edges less that 7degrees(6 in total). I made the mesh fine and also locally controlled the mesh in and around the fin. My results are much more accurate now. A max error of 10% and a standard deviation of 4% whichis really good.
Now I have two problems
1)As the velocity increases, the error is increasing. this is due to free flow occuring.(PIC ATTACHED). how do i modify the geometry to take care of this?It doesnt let me make the external volume any narrower.
the second one I'll post as soon as im able to get a screenshot of what I want to explain
I want to thank you all you have been very helpful. My boss was very impressed with the agreement of the CFD results with experimental data. I also told him about the help I got from here
hey
i attaching 2 photos of the mesh i had used before which helped me get down the max error to 5%
Now here is my second problem
Now i have to deal with heat transfer
along with the fins, i have attached 2 tubes on each side(Shown in CAD model) (p.s. I will be using only 2 fins and not 4 and will accordingly adjust the CAD model)
the tube are hollow
I have created internal flow volume for the tubes( highlighted in the pic)
I have created an external flow volume also (pic attached)
I will be applying slip/symmetry condition on the side which is highlighted in the above external volume pic. I will also apply slip/symmetry to the side directly opposite to it
Im going to apply aluminum to the fins and tube
Water to the inter volume (through the tube)
Air(fixed) to the external volume
Now the boundary contitions
Inlet Air(external volume) : velocity 8m/s, temperature 45Degrees celsius
Outlet air(external volume): pressure 0Pa(gage)
inlet of the water in tubes (internal volume, total 2 of them 😞 velocity 1m/s, temperature 98 degrees celcius
outlet of the water in tubes (internal volume, 2 of them): Not sure: need help on this
Now i want to calculate the temperature of air at the outlet as gets heated due to the fins.
I also want my analysis to consider the effect of choke
That is, if i reduce my fin pitch (distance between the 2 fins) to an insanely small value, the temperature rise of air should be more (instead of less) as due to closely placed fins, the flow of air is choked (probably due to two boundary layers impringing with each other causing further obstruction to flow). How do I take care of this.
Should i use the same solving conditions, i.e. ADV 2 and eddy viscosity (ratio 10) or anything else
Thank you in advance
p.s. The rest of the pics I Am attaching in another post
I have attached the remaining pics.
Take a large step back.
How is your test setup configured? What does teh test lab look like, what sized duct is there? Note that Ext. Volume from CFD cannot be co-planar with geometry (this is outlined in the help) so there will always be a leakage path. If this should not be the case, Build your wind tunnel in CAD and import it with the rest of the geometry.
I would be running K-epsilon or SST rather than manually selecting a given Tubr/lam ratio with Eddy Visc.
To match test resutls you need to be sure we are matching constraints and assumptions as to how and where we are taking measurements
Which advection model should i run along with SSTK-epsilon ?
a particular research used periodic boundary conditions but did the analysis in a different software(Pic attached)
I couldnt understand as to how this will help
Neither could i figure out how to implement the same
If this is a small section of a larger radiator then yes:
We would want the air domain to be generated appropriately such that it would split the gap/cut through in a periodic/patterned fashion
The lateral/sides upstream of the radiator would have Slip/Symm conditions as to not introduce extra pressure drop and represent a large segment of air coming in.
The sides at and downstream of the radiator should be set up with Periodic conditions (we discuss how this is done in the Help)
This will allow for flow that leave the "right" side to enter the "left" side as though there was a patterned array of them. By not having this in your current model we are assuming its just the 1 fold in a wind tunnel
Thanks for the reply
I am unable to understand which sides should i put up as slip and which as periodic. YOu are refering to the side with more width or less width. Could you clear that a bit please.
Also, should i apply the periodic , slip boundarary condition throughtout the mentioned side of the external volume, (from inlet to outlet) or to only a portion of the side
I have changed my approach a bit
i have constructed 3 rechangular channels in CAD (having a wall thickness of 1mm) and have placed them as shown in the pic "Channel"
The left one is the inlet channel
the right one the outlet channel
the middle one is the channel surrounding the fin (lets call it fin channel)
the channels are open on the sides
in using using the void fill tab i have build a surface at the left opening of the inlet channel and at the right opening of the outlet channel
then i have filled the void
now i have assigned Aluminium to the 3 channels, supressed the 3 channels
assigned air (fixed, 45Degrees) to the 'cfdCreated internal volume'
assigned aluminum to the fin, supressed it
I am only dealing with flow, no heat transfer
reffering to the pic 'FIN flow', i am trying to simulate the pressure drop while air passes over one verticle row of fins
Now I am confused as to apply slip symmetry on which face and periodic condition on which face
i feel i should apply the periodic boundary condition on the flow volume in the fin region, only on the 2 wider sides (the sides which are almost parallel to the plane of the paper)(the side along the faint green axis seen in the top picture)
should i apply the slip symmetry condition on the inlet aur volume or the outlet air volume also
and on which sides should i apply it?
Thanks in advance