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

Cavitation in water hydraulic poppet valve

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   January 31, 2019, 08:36
Default Cavitation in water hydraulic poppet valve
  #1
Senior Member
 
Aja
Join Date: Nov 2013
Posts: 496
Rep Power: 15
aja1345 is on a distinguished road
Hi,


I am simulating a water hydraulic poppet valve in order to investigating cavitation phenomenon in that. Also, I am using a paper for verification of this simulation.



Model is 2D, axisymmetric. Mesh is generated by Gambit software. In order to improve the quality of the mesh, the simulated model is divided into three parts(please see the following picture). Part 1 and part 3 are discretized by using map method, and part 2 is discretized by utilizing pave method. According to the paper, The mesh quality of part 2 has a significant effect on the results accuracy due to the high Reynolds number in this part.





My model:





My mesh:





BC is as follows in my work:












How can set "Interracial area concentration"? this is defualt value(0.0001).








here, the value of diameter is default value. I think that this value should change in this simulation. but How value?

Value of pressure contour is good agreement with the paper result. therefore, My result:








and paper result:







when i display vapor volume fraction in Ansys Fluent, I see the vapor in the specified part from the following figure. Location of vapor formation in my result is same with that of that in paper results. But I have a problem with value of vapor fraction contour and the value of my result is greater than value of the paper(please see the following pictures) Why does this happen?


My result:





Paper result:









Thanks.




aja1345 is offline   Reply With Quote

Old   January 31, 2019, 08:38
Default
  #2
Senior Member
 
Aja
Join Date: Nov 2013
Posts: 496
Rep Power: 15
aja1345 is on a distinguished road
Magnify the My mesh in part2:







Residuals are as follows:



More decrease of residuals is not very effect on the result, especially in vapor volume fraction. According to above picture, IAC (Interfacial area concentration) have not good convergence and this is a problem!!!


There is the following BCs in the paper:





The inlet pressure is increased gradually to 14 MPa (14 MPa is the maximum pressure that provided by the pump in the experiment), and the outlet pressure is kept at the atmospheric pressure (gauge pressure is zero in this paper) or increased gradually from 0 to 12 MPa.
aja1345 is offline   Reply With Quote

Old   February 1, 2019, 06:10
Default
  #3
Senior Member
 
Aja
Join Date: Nov 2013
Posts: 496
Rep Power: 15
aja1345 is on a distinguished road
No one help?
aja1345 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
udf for valve closing a pipe using dynamic mesh chem engineer Fluent UDF and Scheme Programming 2 May 13, 2017 10:39
cavitation problem for a vibrating plate in water ndabir FLUENT 1 May 9, 2016 21:08
Centrifugal Pump Cavitation problem or not. ismael.s CFX 13 February 27, 2012 09:00
Terrible Mistake In Fluid Dynamics History Abhi Main CFD Forum 12 July 8, 2002 10:11
uptodate water distribution network fredius,magige,tanzanian,(e.a) Main CFD Forum 0 January 27, 2002 08:10


All times are GMT -4. The time now is 14:46.