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

Gas throttling

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   August 25, 2020, 04:57
Default Gas throttling
  #1
New Member
 
Avksentev Aleksey
Join Date: Apr 2013
Posts: 1
Rep Power: 0
Avksent is on a distinguished road
Good afternoon, dear forum users!

Please help in solving the following problem (test problem, which means conditional): suppose that there is a choke (inner diameter of the main pipe is 100 mm, inner diameter of the choke is 10 mm).



The working medium is gas (Redlich-Kwong model from the CFX library).



Border conditions:
- input - mass flow (0.01 kg / s), total temperature (623 K)
- outlet - average static pressure (1 MPa)
- walls and symmetry
- domain: pressure 1 atm .; Heat Transfer - Total Energy

After solving, the following is obtained:
Pressure (meets expectations):


Speed (let's close our eyes to the huge speeds for now):


Temperature (...):


The result of the solution seems strange to me - I expected to see a temperature drop not only in the choke, but also behind it (compared to the gas temperature at the inlet), as it happens in real throttling devices behind which sections of the pipeline can be covered with frost.

The temperature pattern along the central axis - behind the throttle was restored:


Please point me to my mistakes in assumption / modeling.
Avksent is offline   Reply With Quote

Old   August 25, 2020, 06:52
Default
  #2
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,715
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
Please post images directly on the forum and do not use third party download sites.

To answer your question: Accuracy is an FAQ: https://www.cfd-online.com/Wiki/Ansy..._inaccurate.3F

Have you calculated what temperature loss you expect? Have you looked at your results carefully to get the exact temperature loss predicted by your model?
__________________
Note: I do not answer CFD questions by PM. CFD questions should be posted on the forum.
ghorrocks is offline   Reply With Quote

Old   August 26, 2020, 07:27
Default
  #3
Member
 
Henrique Stel
Join Date: Apr 2009
Location: Curitiba, Brazil
Posts: 93
Rep Power: 17
Stel is on a distinguished road
Did you get any warning message during solution regarding the enthalpy calculation bounds? (I see that you are not generating table interpolation in the EOS)
Stel is offline   Reply With Quote

Reply

Tags
joule thomson


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
Setting the height of the stream in the free channel kevinmccartin CFX 12 October 13, 2022 21:43
Domain Reference Pressure and mass flow inlet boundary AdidaKK CFX 75 August 20, 2018 05:37
error message cuteapathy CFX 14 March 20, 2012 06:45
Constant velocity of the material Sas CFX 15 July 13, 2010 08:56
Gas pressure question Dan Moskal Main CFD Forum 0 October 24, 2002 22:02


All times are GMT -4. The time now is 08:57.