|
[Sponsors] |
Questions about pressure calculation on buoyancy flow(thermal stratified flow) |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
March 19, 2014, 03:31 |
Questions about pressure calculation on buoyancy flow(thermal stratified flow)
|
#1 |
Member
Ben B. Huang
Join Date: Oct 2012
Posts: 54
Rep Power: 14 |
Hey guys,
I am stuck on the problem to compute the pressure distribution of buoyancy flow, a large reservoir with temperature stratification. The CFX theory/modeling Guide says: "For buoyancy calculation, a source term is added to the momentum equations as follows: S_m,buoy = (rho - rho_ref)*g. When buoyancy model is activated, the pressure in the momentum equation excludes the hydrostatic gradient due to rho_ref. This pressure is related to the absolute pressure as follows: P_abs = P + P_ref + rho_ref*g(r - r_ref) where r_ref is a reference location." I learned that 'pressure' at the inlet boundary can be computed from equation like this 'integration dP =Integration (rho - rho_ref)*g dz' where z is the depth direction. See the picture as well. The model is simplified as shown in the figure. The tank has a vertical temperature stratification(i.e. temperature is a function with regard to depth), and the density is a function of temperature, and the pressure is relevant with the density but I am not sure how to calculate. So, my question is, how can I set the static pressure at the inlet boundary? Does it matter to the results? I computed the pressure using the method in the figure, and the simulation is not converged. I do not figure out the problem. Any suggestions? I will very appreciate your help. Thank you very much. |
|
March 19, 2014, 06:49 |
|
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
If you are defining pressure then can't you use a single constant value over the entire inlet? As the documentation says that hydrostatic pressure component has been taken out of the pressure variable.
|
|
March 19, 2014, 09:11 |
|
#3 | |
Member
Ben B. Huang
Join Date: Oct 2012
Posts: 54
Rep Power: 14 |
Quote:
Thank you so much. |
||
March 19, 2014, 09:22 |
|
#4 |
Member
Ben B. Huang
Join Date: Oct 2012
Posts: 54
Rep Power: 14 |
another question:
consider no thermal stratification, inlet pressure can be set to constant? I did that before. I want to confirm that. Thank you! |
|
March 19, 2014, 17:37 |
|
#5 | |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
Quote:
Yes, the inlet can be set to a constant with no thermal stratification as well. You should just try these options and find this all out for yourself. |
||
March 19, 2014, 20:45 |
|
#6 |
Member
Ben B. Huang
Join Date: Oct 2012
Posts: 54
Rep Power: 14 |
I see.
Thank you so much. |
|
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Total pressure and mass flow boundary condition at inlet | bscphil | OpenFOAM Pre-Processing | 3 | July 9, 2017 15:39 |
Mass flow inlet and pressure outlet issue | nikhil | FLUENT | 5 | December 11, 2013 13:30 |
Maintaining Static Pressure at Fluid Flow Inlet | cdevalve | FLUENT | 3 | January 14, 2012 01:11 |
Non-steady flow simplified for use in Vissim | steamerandy | Main CFD Forum | 0 | October 31, 2011 22:08 |
Pressure Drop Calculation | mk_mard | STAR-CCM+ | 3 | August 29, 2011 03:06 |