CFD Online Logo CFD Online URL
www.cfd-online.com
[Sponsors]
Home > Forums > Software User Forums > ANSYS > CFX

Multiphase Phase Change

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   December 10, 2018, 23:14
Default Multiphase Phase Change
  #1
Senior Member
 
Pedro Oliveira
Join Date: Feb 2018
Location: Portugal
Posts: 109
Rep Power: 8
oliveira1820 is on a distinguished road
I´m modelling water/steam (IAWPS) phase change with Thermal Phase Change Model and even with 600 W distributed in only a 3 cm cone, the max temperature I obtain it isn´t enough to form steam. The recipient after equilibrium only presents liquid water as ~100 % volume fraction.

I can´t undesrtand what´s happening. Does anyone had a similar problem?
oliveira1820 is offline   Reply With Quote

Old   December 11, 2018, 05:37
Default
  #2
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
Either you have not put enough heat into the water to boil it or you have a numerical error which is grossly underestimating the heat transfer. It would detailed analysis of your simulation to work out which, and the forum is not the place to do that sort of thing.

If you posted your geometry and output file we can have a look at your setup and see if we can see any obvious problems.
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Old   December 11, 2018, 22:36
Default
  #3
Senior Member
 
Pedro Oliveira
Join Date: Feb 2018
Location: Portugal
Posts: 109
Rep Power: 8
oliveira1820 is on a distinguished road
I´l start by posting my heat source, I want it to be distributed with different values for each cylinder (to simulate bragg peak heat deposition from a cylinder energy beam), resulting in the sum of 639 W:

The recipient has the referencial at x=0, y=0 and z=0. I consider the cylinder along the z direction.


This is my CEL:

valorx = abs(x)
valory = abs(y)

limitxy = 0.0045 [m] #cylinder radius

sourcex = if (valorx < limitxy, 1, 0)

sourcey = if (valory < limitxy, 1, 0)

limitz1 = 0.0025[m] # different consecutive cylinders range
limitz2 = 0.011[m]
limitz3 = 0.0155[m]
limitz4 = 0.02[m]
limitz5 = 0.02225[m]


sourcez1 = if (z<limitz1, 1, 0)
sourcez2 = if( z>limitz1, if (z<limitz2, 1, 0) , 0)
sourcez3 = if( z>limitz2, if (z<limitz3, 1, 0) , 0)
sourcez4 = if( z>limitz3, if (z<limitz4, 1, 0) , 0)
sourcez5 = if( z>limitz4, if (z<limitz5, 1, 0) , 0)


sourcetotal1 = sourcex*sourcey*sourcez1
sourcetotal2 = sourcex*sourcey*sourcez2
sourcetotal3 = sourcex*sourcey*sourcez3
sourcetotal4 = sourcex*sourcey*sourcez4
sourcetotal5 = sourcex*sourcey*sourcez5

Sourcefluido = (sourcetotal1*106.65+ sourcetotal2*114.18 + sourcetotal3*114.49 + sourcetotal4*125.04 + sourcetotal5*178.64) [kg m^2 s^-3] #Total Source applied to my full domain with different energy for each one


END


The recipient has initially 80% liquid water and 20% steam, the source is a Bulk Source (Use Volume Fraction) (Total Source).

Does it seem good for you? Do the 639 W get deposited this way evenly in both fluids (considering the olume fraction inside each cylinder) in each cylinder and 639W summed?
oliveira1820 is offline   Reply With Quote

Old   December 11, 2018, 23:47
Default
  #4
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
You don't need to do all that stuff if you just define a mesh region then define that mesh region as a subdomain which you apply your source to.

You should check that your source term results in 639W of heating as you intend. Check that the temperature is rising at the expected rate.

I cannot answer your other questions without seeing your geometry as I have no idea what you are modelling.
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Old   December 12, 2018, 00:01
Default
  #5
Senior Member
 
Pedro Oliveira
Join Date: Feb 2018
Location: Portugal
Posts: 109
Rep Power: 8
oliveira1820 is on a distinguished road
I´l try to do the cylinders as mesh regions and apply a source to each one and I´l comeback with feeedback

I need to design the areas on AutoCad first right?
oliveira1820 is offline   Reply With Quote

Old   December 12, 2018, 00:09
Default
  #6
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
The easiest way is to define them as separate regions in the mesh. So you might be able to do that in your meshing package, or you might need to do it in your solid modelling package depending on your setup.
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Old   December 12, 2018, 02:54
Default
  #7
Senior Member
 
Pedro Oliveira
Join Date: Feb 2018
Location: Portugal
Posts: 109
Rep Power: 8
oliveira1820 is on a distinguished road
But I have a doubt, if I design a cubic domain and then cylinders inside the cube. How can I say to the software that the cylinders are sub-domain of the cubes to make the sources in the cylinders, and the water just exist in the cube? Because if I consider all on the same domain, the space ocupied by the cylinders overlaps with the cube and software end in error, cause water is on both twice.

Or is it another way of telling the software that I want the source inside the cylinders, that is using only cylinders geometry as reference to the energy sources, and ignore them o the rest.
oliveira1820 is offline   Reply With Quote

Old   December 12, 2018, 05:53
Default
  #8
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
The solids must not overlap. So if you generate cylinders in the middle of your domain you must remove those cylindrical regions from the outer region.
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Reply


Posting Rules
You may not post new threads
You may not post replies
You may not post attachments
You may not edit your posts

BB code is On
Smilies are On
[IMG] code is On
HTML code is Off
Trackbacks are Off
Pingbacks are On
Refbacks are On


Similar Threads
Thread Thread Starter Forum Replies Last Post
Phase Change in VOF Evaporation/Condensation Models yoshiurr STAR-CCM+ 3 March 21, 2019 07:12
Need help to Simulate Phase change of Water liquid after mixing with Hot Air Stream diineshns FLUENT 0 March 17, 2018 06:14
Why opening boundary for multiphase simulation must set Volume Fraction of each phase TerryNiu CFX 2 March 13, 2018 06:49
Pressure Outlet for phase change simulation dinesh FLUENT 0 November 21, 2013 23:50
Wich solver for CHT, multiphase et phase change? micpage18 OpenFOAM Running, Solving & CFD 3 August 5, 2013 11:48


All times are GMT -4. The time now is 12:16.