|
[Sponsors] |
specific heat capacity changing with temperature |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
July 12, 2012, 12:41 |
specific heat capacity changing with temperature
|
#1 |
Member
Ahmet
Join Date: Mar 2011
Location: Ankara/ Turkey
Posts: 37
Rep Power: 15 |
Dear all,
I have a case that specific hat capacity changes with temperature. After solver manager starts , I get this failure. What can I do to solve this problem? +--------------------------------------------------------------------+ | Initial Conditions Supplied by Fields in the Input Files | +--------------------------------------------------------------------+ Domain Name : ICEngine Mesh Coordinates +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Specific heat information for fluid component "C7H16l" is either | | missing or invalid. Supported formats are: NASA polynomials, Zero | | pressure polynomials or constant values for the specific heat. | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | Writing crash recovery file | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | ERROR #001100279 has occurred in subroutine ErrAction. | | Message: | | Stopped in routine SU_PROP | | | | | | | | | | | +--------------------------------------------------------------------+ +--------------------------------------------------------------------+ | An error has occurred in cfx5solve: | | | | The ANSYS CFX solver exited with return code 1. No results file | | has been created. | +--------------------------------------------------------------------+ End of solution stage. |
|
July 12, 2012, 19:02 |
HI
|
#2 |
Senior Member
Danial
Join Date: Nov 2011
Posts: 179
Rep Power: 15 |
How did you define your Cp as function of time, I mean which format?Because ERROR clearly describes the allowable formats, you can use. If you have specified as expression then post it here.
Thanks |
|
July 12, 2012, 20:29 |
|
#3 |
Member
Ahmet
Join Date: Mar 2011
Location: Ankara/ Turkey
Posts: 37
Rep Power: 15 |
I defined Cp as a function of temperature. I imported a table that shows Cp changes with temperature.
|
|
July 13, 2012, 00:31 |
HI
|
#4 |
Senior Member
Danial
Join Date: Nov 2011
Posts: 179
Rep Power: 15 |
Then this error clearly states that your table has some problem (i.e format/coding error) because solver is unable to read it. Without looking at your table, i cant be sure about anything. But you may use Polynomials format by developing an equation or writing a CEL Expression. Have you selected the real gas (EOS) option for your material because I guess table format is supported only for real gas problems. These all are possibilities, i can think of right now.
Last edited by Danial Q; July 13, 2012 at 01:00. |
|
July 13, 2012, 05:37 |
|
#5 |
Member
Ahmet
Join Date: Mar 2011
Location: Ankara/ Turkey
Posts: 37
Rep Power: 15 |
Here is an example of my table. I have imported this table and if my values are out of the table, it must be extrapolate. Is there something wrong about my table?
Temperature (K) Cp (J/g*K) 186,72 1,9651 188,81 1,9673 190,9 1,9695 192,99 1,9718 195,07 1,9743 197,16 1,9768 199,25 1,9794 201,34 1,9821 203,42 1,985 205,51 1,9879 |
|
July 13, 2012, 21:21 |
HI
|
#6 |
Senior Member
Danial
Join Date: Nov 2011
Posts: 179
Rep Power: 15 |
I already told you that (.rgp) format table is used to define some real gas properties of user material. So, you can add that table by choosing material properties option to table and filling component and file name. Else, you can just use ZERO pressure POLYNOMIAL if your Cp and Enthalpy of materials are only function of temps. In my opinion, it would suit you the best.
For more details you can just read ansys cfd solver theory guide and tutorials. Cheers |
|
July 14, 2012, 06:03 |
|
#7 |
Member
Ahmet
Join Date: Mar 2011
Location: Ankara/ Turkey
Posts: 37
Rep Power: 15 |
Dear Danial, I have found that information that If I want to choose heat capacity changing with temperature, I have to use Nasa polynomials. So I' m trying to use Nasa polynomials. Thank you for your help.
|
|
July 16, 2012, 13:25 |
|
#8 |
Member
Join Date: Dec 2009
Posts: 44
Rep Power: 17 |
Dear Ahmet,
is the Cp you are trying to define being applied to a particle phase, by any chance? CG |
|
July 17, 2012, 03:12 |
|
#9 |
Member
Ahmet
Join Date: Mar 2011
Location: Ankara/ Turkey
Posts: 37
Rep Power: 15 |
dear cfdgremlin,
I couldn' t define cp from table values but I' m using Nasa Polynomials now. |
|
December 12, 2012, 17:25 |
|
#10 |
Senior Member
Saima
Join Date: Apr 2009
Location: Canada
Posts: 185
Rep Power: 16 |
Could you pls tell me how you implemented polynomial for specific heat capacity in CFX pre?
__________________
Best Redards, Saima |
|
October 6, 2015, 19:15 |
|
#11 |
New Member
ana
Join Date: Jul 2013
Posts: 7
Rep Power: 13 |
||
October 7, 2015, 02:24 |
|
#12 |
Senior Member
Join Date: Feb 2011
Posts: 496
Rep Power: 18 |
||
October 7, 2015, 12:36 |
|
#13 |
New Member
ana
Join Date: Jul 2013
Posts: 7
Rep Power: 13 |
||
October 7, 2015, 12:44 |
|
#14 |
Senior Member
Join Date: Jun 2009
Posts: 1,880
Rep Power: 33 |
You are asking in the wrong forum
|
|
October 8, 2015, 01:13 |
|
#15 |
Senior Member
Join Date: Feb 2011
Posts: 496
Rep Power: 18 |
||
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
mass flow in is not equal to mass flow out | saii | CFX | 12 | March 19, 2018 06:21 |
Wall Heat Flux & Temperature | Greg Perkins | FLUENT | 10 | November 20, 2015 10:32 |
Calculation of the Governing Equations | Mihail | CFX | 7 | September 7, 2014 07:27 |
Two-Phase Buoyant Flow Issue | Miguel Baritto | CFX | 4 | August 31, 2006 13:02 |
VISCOUS heat dissipation | Joseph | CFX | 0 | October 1, 2004 09:52 |