|
[Sponsors] |
June 16, 2014, 21:31 |
Error in phase change simulation
|
#1 |
New Member
Join Date: May 2014
Posts: 7
Rep Power: 12 |
----------------------------------
Error in subroutine FNDVAR : Error finding variable DENSAT_FL1 GETVAR originally called by subroutine cal_DIAM +--------------------------------------------------------------------+ | Writing crash recovery file | +--------------------------------------------------------------------+ Details of error:- ---------------- Error detected by routine MAKDIR CDRNAM = cal_IPTC CRESLT = OLD Current Directory : /FLOW/SOLUTION/TSTEP5/CLOOP1/ZN1/VERTICES |
|
June 29, 2014, 17:07 |
|
#2 |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
Hi,
I am getting the same error, have you found any solution to this? Regards |
|
June 29, 2014, 20:24 |
|
#3 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,841
Rep Power: 144 |
CFX error messages can be a bit cryptic. I think this one is saying you have not defined the saturation properties (maybe density) for a phase.
|
|
June 29, 2014, 20:30 |
|
#4 |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
Dear Gorrocks,
Thanks for the reply, I am using predefined materials, "Liquid Water" and "Water Ideal Gas", density of Water in gas phase cannot be defined manually, as it is compressible and density is computed by CFX according to temp. press. conditions. I donot see other place where the density should be defined. I am using "Water Ideal Gas" as continuous fluid, and Water Liquid as Droplets(Phase change) , if i change Dispersed Liquid , the problem goes away. But i need Phase change here! Regards |
|
June 30, 2014, 09:59 |
|
#5 | |
Senior Member
Mr CFD
Join Date: Jun 2012
Location: Britain
Posts: 361
Rep Power: 15 |
Quote:
Phase change simulations are not easy. There is a ton of literature to read before you even think about attempting a "simple" phase change simulation. The best advice is: read the CFX theory and user guides. And then read them again. Complete the Bartolomej boiling test case in CFX to get you started. You can get the files from Ansys. |
||
June 30, 2014, 22:57 |
|
#6 | |
New Member
Join Date: May 2014
Posts: 7
Rep Power: 12 |
Quote:
|
||
July 2, 2014, 21:02 |
|
#7 |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
@ tomide,
Dear i think you are not using proper materials for Phase Change, i have switched to H20v,H20l and i have resolved that error (That error DENSAT... means that Saturation Density not found), You need to use a pair of materials which have well defined saturation properties in CFX. And... This is my interpretation. |
|
August 18, 2014, 22:47 |
help
|
#8 | |
New Member
Julia
Join Date: May 2011
Posts: 20
Rep Power: 15 |
Quote:
I have a problem with phase change (droplet), I find H2Ol in CFX material, but cannot find H2Ov! Can I ask you where you find it? I built this material from new material, but the error that ‘Error finding variable PSAT’ is appeared! Could you help me please? Regards |
||
August 19, 2014, 12:32 |
|
#9 | |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
Quote:
That is a mistake in my above comment, Sorry for the confusion it created. The Liquid and Gas phase water materials are H2Ol and H20 (Not H2Ov) respectively, and their Homogeneous Binary Mixture is named as H20vl. You can find these materials in "Water Data" or "Interphase mass transfer" groups. Please note that, you would have to import all three to your materials list; H2Ol, H2O , H2Ovl. That error about PSAT means that Saturation Pressure was not found. Importing all the three materials would correct this Inshallah ! Personally i am now using IAPWS-IF97 water and steam data for my simulations , i found it better and it is also available within CFX. Hope that helps! Regards, Mudassir Farooq |
||
August 22, 2014, 05:00 |
|
#10 |
New Member
Julia
Join Date: May 2011
Posts: 20
Rep Power: 15 |
Dear Mudassir
Thanks for your help, I used materials in IAPWS-IF97 , but this error appear: ‘Independent variables were clipped during table generation’ I don’t understand this message, which item I must change it? Thanks a lot for your help |
|
August 22, 2014, 07:29 |
|
#11 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,841
Rep Power: 144 |
In the materials tab you expand out a few levels and there is some options for table generation.
|
|
August 22, 2014, 09:39 |
|
#12 | |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
Quote:
First i would like to explain what does this error mean so that you can have a deeper understanding. When you start a simulation the CFX-Solver generates the tables of the properties (density, viscosity etc) for different temperature and pressure values, Then during the simulation solver will pick the property value from these tables. This process of making tables is called "TABLE GENERATION". CFX by default generates these table from 273K - 500 K (i dont remember exactly values) in steps of 5 degrees or similar. Now your error means that the temperatures and pressure values in your simulation are outside the default table range. It is always recommended to to provide Table range manually according to the temperature and pressure EXTREMES in the simulation to avoid this error. Now to input table range: Double click the your material in Outline -> Tick TABLE GENERATION under Material Properties tab -> Tick Minimum Temp., Max. Temp , Min Pressure, Max Press and Number of points and provide values for all of these. -- Do Not Check mark the Extrapolation. Sorry for being lengthy, too descriptive! Hope that helps! Regards, Mudassir Farooq |
||
August 22, 2014, 10:47 |
|
#13 | |
New Member
Julia
Join Date: May 2011
Posts: 20
Rep Power: 15 |
Quote:
Hi Mudassir My problem is solved and the error is eliminated, thanks for your help I wish the best for you! Best Regards |
||
September 3, 2014, 15:08 |
|
#14 |
New Member
Julia
Join Date: May 2011
Posts: 20
Rep Power: 15 |
Hi Mudassir
Can I ask you a question? do you simulate wet steam flow in CFX? if your answer is positive, can I ask you some question? Thanks Julia |
|
September 4, 2014, 11:11 |
|
#15 |
New Member
Mudassir
Join Date: Apr 2014
Location: Pakistan
Posts: 11
Rep Power: 12 |
Hi Julia,
Yes I did simulate wet steam, Actually i vaporized water in my system and the steam you get would be wet steam unless you superheat it. You may ask the questions, May be i could answer. Mudassir Farooq |
|
May 28, 2015, 08:56 |
|
#16 | |
Member
Adil Syyed
Join Date: May 2012
Posts: 49
Rep Power: 14 |
Quote:
Sorry for bringing up an old post. In phase change simulation, say direct contact condensation, do we have to import all the three materials i.e. H2O, H2Ol and H2Ov, as you mentioned. Shouldn't two materials H2O and H2Ol do? If I import the third material H2Ov then I have to define it as Continuous/dispersed liquid. It kind of becomes a 3rd phase. Regards |
||
May 28, 2015, 09:51 |
|
#17 |
Senior Member
Join Date: Jun 2009
Posts: 1,865
Rep Power: 33 |
Be careful not confuse "materials" with "phases" when using ANSYS CFX.
"Materials" describe the thermodynamic state, properties of a substance. "Phases" are how you want these substances to be modeled. For example, you can import MatLiquid, MatVapor, MatBinMixture materials. Then you decide how to model the physics: 1 - Single phase using a homogeneous binary mixture: you assign the MatBinMixture to the unique phase in the model. 2 - Single phase using the vapor state: you assing the MatVapor material to the unique phase in the model. Similar if you decide to model the liquid with MatLiquid 3 - Multiphase modeling using independent phases: you assign MatVapor to a phase (and the appropriate morphology), and you assign MatLiquid to another phase (and its morphology as well). Summary: you can import as many materials as you want, you then create phases as your modeling needs require. Hope the above helps, |
|
May 28, 2015, 09:58 |
|
#18 | |
Member
Adil Syyed
Join Date: May 2012
Posts: 49
Rep Power: 14 |
Quote:
|
||
March 19, 2016, 06:33 |
|
#19 |
New Member
abubakar izhar
Join Date: Oct 2015
Posts: 9
Rep Power: 11 |
have someone tried the Bartolomej subcooled boiling test provided by ansys. i want to know wether the wall boiling model can be applied at low pressure of 3 bar or not. moreover how has ansys input bubble diameter expression in this case.can someone guide to provide input at 3 bar.
|
|
August 31, 2018, 16:43 |
I am also finding difficulty in the boiling simulations
|
#20 | |
Member
Soumitra Vadnerkar
Join Date: Aug 2018
Posts: 70
Rep Power: 8 |
Quote:
You are right JuPa I am also finding difficulty in the boiling simulations. |
||
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Phase change from liquid to vapor in a nozzle | SebastianSchuster | CFX | 6 | September 28, 2015 23:02 |
Change operating pressure without redoing simulation | pakk | FLUENT | 0 | November 29, 2013 05:00 |
modeling phase change and homogeneous bubbles in many cycles | dwtme | FLOW-3D | 12 | January 1, 2013 05:57 |
Phase Change Heat Conduction | hawkeye321 | OpenFOAM | 14 | April 30, 2011 15:24 |
Flash Process / Problem with thermal phase change model | Ridley | CFX | 0 | July 21, 2010 08:57 |