|
[Sponsors] |
Wall Transfer Coefficien - Heat Transfer Coefficient - CFX |
|
LinkBack | Thread Tools | Search this Thread | Display Modes |
November 2, 2011, 18:49 |
Wall Transfer Coefficien - Heat Transfer Coefficient - CFX
|
#1 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
Dear friends,
I have simulated the flow in a simple geometry (like 2 paralel walls - "2,5D" case). My BC are (for laminar flow): In - low velocity and fixed temperature; Wall - no slip and fixed temperature; Out - Openning with static pressure. In CFX-Post: I have created a line in wall position, through the length. When I plot the variable (Wall Transfer Coefficien), the value found isn't the value hoped. 1) Why this happen? But when I take the Heat Flow "q" (in same line created) and temperature average of section "Tav" (with formulas in own CFX-Post)... I can obtain "h" correctly: q /(Tw-Tav) = h 2) Why "q" is correct, but "h" isn't? 3) How can I obtain "h" directly? 4) I have seen thread about that. Some users has talked about reference temperature.. But I don't understand that... Someone can explain it for me? and how can I change this reference temperature? I'm starting to study the CFD world... Thanks in advance everyone. |
|
November 2, 2011, 21:58 |
|
#2 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
||
November 2, 2011, 23:25 |
|
#3 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
First of all, thanks for answer.
I liked the link! There are a lot of good things over there! but... don't worry... I have done all steps, mainly for to learn how the software works. My results aren't inaccurate. I'm using: RMS = 10^-09 and highresolution for advection and couple velocity-pressure. The simulation doesn't need great adjustments.. So highresolution scheme is good. I have problem just with Heat Transfer Coefficient, even the "q" seem is right. The manual doesn't let clear about "h". There said some thing about: "... using an external heat transfer coefficient, hc...". As am I getting the value of "q" correct, while the value of "h" seem being wrong? How can I obtain the truly value of "h"? *I did the same simulation on FLUENT software and I obtained the "h" correct there! Last edited by Gargioni; November 2, 2011 at 23:34. Reason: I forgot some things =/ |
|
November 2, 2011, 23:49 |
|
#4 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
There is more to accuracy than convergence tolerance and differencing scheme.
h is referenced to a ambient temperature. By default CFX uses a function of the local fluid temperature which is usually quite different to the engineering definition (which is usually inlet temperature or far field temperature). To get h as engineers understand it have a look in the output file. There is a discussion in there about HTC reference temperatures and how to define your own temperature. |
|
November 3, 2011, 00:25 |
|
#5 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
"There is more to accuracy than convergence tolerance and differencing scheme." I said just for let clear that I don't have problems with accuracy.
May you help me to find this thread about HTC? Thanks in advance =] |
|
November 3, 2011, 00:28 |
|
#6 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
It is in the output file. Have a look in your simulation. It is not a thread, but there are plenty of threads in the forum which have discussed the issue.
|
|
November 4, 2011, 16:34 |
|
#7 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
I changed the expert parameter tbulk for htc. And I think CFX considers the tbulk value like constant
How I said: I have simulated the flow in a simple geometry, like 2 paralel walls - "2,5D" case. I have created a line in wall position, through the length, for captures the "h", however the value of "tbulk" is variable along the length. What can I do when the tbulk value isn't constant? |
|
November 6, 2011, 05:57 |
|
#8 |
Super Moderator
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,870
Rep Power: 144 |
If you have set the tbulk parameter then tbulk will be constant and the value you define, otherwise it will depend on local flow conditions.
You can easily extract h for a constant tbulk anyway. The local tbulk temperature used is an available variable, so between that and the wall heat transfer variable you can calculate h based on any tbulk you like. |
|
March 7, 2012, 01:19 |
|
#9 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
I solved my problem... doing a CEL routine.
__________________
-- Gregory T. Gargioni ------><> E-mail: gargionis <at> gmail "dot" com ------------------------------------- |
|
April 15, 2013, 08:46 |
|
#10 |
Member
Join Date: Nov 2011
Location: Germany
Posts: 40
Rep Power: 15 |
maybe u can give a short summary of the steps which u made to help me?
|
|
October 24, 2017, 15:02 |
|
#11 |
New Member
Join Date: Oct 2011
Posts: 7
Rep Power: 15 |
!$Tw=298.15;
!$Zposi = 0.4; !$TBulkZ = $Zposi*20; !$a=0; !for ($i=1; $i<89; $i++) { !$a=$a+0.005; !$Xposi[$i] = $a; !} !for ($i=1; $i<89; $i++) { PLANE: Teste.$i Option = XY Plane Z = $Xposi[$i] Colour Mode = Variable Colour Variable = Temperature Range = Local END !$Tbulk[$i] = massFlowAve("Temperature","Teste.$i"); !$q[$i] = massFlowAve("Wall Heat Flux","Teste.$i"); !$h[$i]=($q[$i]/($Tw-$Tbulk[$i])); !} !$b=0; !for ($i=1; $i<41; $i++) { !$b=$b+0.0001875; !$Yposi[$i] = $b; !} !for ($i=1; $i<41; $i++) { POINT: Point.$i Option = XYZ Point = 0.0, $Yposi[$i], $Zposi Colour Mode = Variable Colour Variable = Temperature Range = Global END !$T[$i] = maxVal("Temperature","Point.$i"); !$Tadm[$i] = ($Tw-$T[$i])/($Tw-$Tbulk[$TBulkZ]) !} $Tbulk[1] $q[1] $h[1] $Xposi[1] $Tbulk[2] $q[2] $h[2] $Xposi[2] $Tbulk[3] $q[3] $h[3] $Xposi[3] $Tbulk[4] $q[4] $h[4] $Xposi[4] $Tbulk[5] $q[5] $h[5] $Xposi[5] $Tbulk[6] $q[6] $h[6] $Xposi[6] $Tbulk[7] $q[7] $h[7] $Xposi[7] $Tbulk[8] $q[8] $h[8] $Xposi[8] $Tbulk[9] $q[9] $h[9] $Xposi[9] $Tbulk[10] $q[10] $h[10] $Xposi[10] $Tbulk[11] $q[11] $h[11] $Xposi[11] $Tbulk[12] $q[12] $h[12] $Xposi[12] $Tbulk[13] $q[13] $h[13] $Xposi[13] $Tbulk[14] $q[14] $h[14] $Xposi[14] $Tbulk[15] $q[15] $h[15] $Xposi[15] $Tbulk[16] $q[16] $h[16] $Xposi[16] $Tbulk[17] $q[17] $h[17] $Xposi[17] $Tbulk[18] $q[18] $h[18] $Xposi[18] $Tbulk[19] $q[19] $h[19] $Xposi[19] $Tbulk[20] $q[20] $h[20] $Xposi[20] $Tbulk[21] $q[21] $h[21] $Xposi[21] $Tbulk[22] $q[22] $h[22] $Xposi[22] $Tbulk[23] $q[23] $h[23] $Xposi[23] $Tbulk[24] $q[24] $h[24] $Xposi[24] $Tbulk[25] $q[25] $h[25] $Xposi[25] $Tbulk[26] $q[26] $h[26] $Xposi[26] $Tbulk[27] $q[27] $h[27] $Xposi[27] $Tbulk[28] $q[28] $h[28] $Xposi[28] $Tbulk[29] $q[29] $h[29] $Xposi[29] $Tbulk[30] $q[30] $h[30] $Xposi[30] $Tbulk[31] $q[31] $h[31] $Xposi[31] $Tbulk[32] $q[32] $h[32] $Xposi[32] $Tbulk[33] $q[33] $h[33] $Xposi[33] $Tbulk[34] $q[34] $h[34] $Xposi[34] $Tbulk[35] $q[35] $h[35] $Xposi[35] $Tbulk[36] $q[36] $h[36] $Xposi[36] $Tbulk[37] $q[37] $h[37] $Xposi[37] $Tbulk[38] $q[38] $h[38] $Xposi[38] $Tbulk[39] $q[39] $h[39] $Xposi[39] $Tbulk[40] $q[40] $h[40] $Xposi[40] $Tbulk[41] $q[41] $h[41] $Xposi[41] $Tbulk[42] $q[42] $h[42] $Xposi[42] $Tbulk[43] $q[43] $h[43] $Xposi[43] $Tbulk[44] $q[44] $h[44] $Xposi[44] $Tbulk[45] $q[45] $h[45] $Xposi[45] $Tbulk[46] $q[46] $h[46] $Xposi[46] $Tbulk[47] $q[47] $h[47] $Xposi[47] $Tbulk[48] $q[48] $h[48] $Xposi[48] $Tbulk[49] $q[49] $h[49] $Xposi[49] $Tbulk[50] $q[50] $h[50] $Xposi[50] $Tbulk[51] $q[51] $h[51] $Xposi[51] $Tbulk[52] $q[52] $h[52] $Xposi[52] $Tbulk[53] $q[53] $h[53] $Xposi[53] $Tbulk[54] $q[54] $h[54] $Xposi[54] $Tbulk[55] $q[55] $h[55] $Xposi[55] $Tbulk[56] $q[56] $h[56] $Xposi[56] $Tbulk[57] $q[57] $h[57] $Xposi[57] $Tbulk[58] $q[58] $h[58] $Xposi[58] $Tbulk[59] $q[59] $h[59] $Xposi[59] $Tbulk[60] $q[60] $h[60] $Xposi[60] $Tbulk[61] $q[61] $h[61] $Xposi[61] $Tbulk[62] $q[62] $h[62] $Xposi[62] $Tbulk[63] $q[63] $h[63] $Xposi[63] $Tbulk[64] $q[64] $h[64] $Xposi[64] $Tbulk[65] $q[65] $h[65] $Xposi[65] $Tbulk[66] $q[66] $h[66] $Xposi[66] $Tbulk[67] $q[67] $h[67] $Xposi[67] $Tbulk[68] $q[68] $h[68] $Xposi[68] $Tbulk[69] $q[69] $h[69] $Xposi[69] $Tbulk[70] $q[70] $h[70] $Xposi[70] $Tbulk[71] $q[71] $h[71] $Xposi[71] $Tbulk[72] $q[72] $h[72] $Xposi[72] $Tbulk[73] $q[73] $h[73] $Xposi[73] $Tbulk[74] $q[74] $h[74] $Xposi[74] $Tbulk[75] $q[75] $h[75] $Xposi[75] $Tbulk[76] $q[76] $h[76] $Xposi[76] $Tbulk[77] $q[77] $h[77] $Xposi[77] $Tbulk[78] $q[78] $h[78] $Xposi[78] $Tbulk[79] $q[79] $h[79] $Xposi[79] $Tbulk[80] $q[80] $h[80] $Xposi[80] $Tbulk[81] $q[81] $h[81] $Xposi[81] $Tbulk[82] $q[82] $h[82] $Xposi[82] $Tbulk[83] $q[83] $h[83] $Xposi[83] $Tbulk[84] $q[84] $h[84] $Xposi[84] $Tbulk[85] $q[85] $h[85] $Xposi[85] $Tbulk[86] $q[86] $h[86] $Xposi[86] $Tbulk[87] $q[87] $h[87] $Xposi[87] $Tbulk[88] $q[88] $h[88] $Xposi[88] $Tbulk[89] $q[89] $h[89] $Xposi[89] $Tbulk[90] $q[90] $h[90] $Xposi[90] $Tbulk[91] $q[91] $h[91] $Xposi[91] $Tbulk[92] $q[92] $h[92] $Xposi[92] $Tbulk[93] $q[93] $h[93] $Xposi[93] $Tbulk[94] $q[94] $h[94] $Xposi[94] $Tbulk[95] $q[95] $h[95] $Xposi[95] $Tbulk[96] $q[96] $h[96] $Xposi[96] $Tbulk[97] $q[97] $h[97] $Xposi[97] $Tbulk[98] $q[98] $h[98] $Xposi[98] $Tbulk[99] $q[99] $h[99] $Xposi[99] $Tbulk[100] $q[100] $h[100] $Xposi[100] $Yposi[1] $Tadm[1] $Yposi[2] $Tadm[2] $Yposi[3] $Tadm[3] $Yposi[4] $Tadm[4] $Yposi[5] $Tadm[5] $Yposi[6] $Tadm[6] $Yposi[7] $Tadm[7] $Yposi[8] $Tadm[8] $Yposi[9] $Tadm[9] $Yposi[10] $Tadm[10] $Yposi[11] $Tadm[11] $Yposi[12] $Tadm[12] $Yposi[13] $Tadm[13] $Yposi[14] $Tadm[14] $Yposi[15] $Tadm[15] $Yposi[16] $Tadm[16] $Yposi[17] $Tadm[17] $Yposi[18] $Tadm[18] $Yposi[19] $Tadm[19] $Yposi[20] $Tadm[20] $Yposi[21] $Tadm[21] $Yposi[22] $Tadm[22] $Yposi[23] $Tadm[23] $Yposi[24] $Tadm[24] $Yposi[25] $Tadm[25] $Yposi[26] $Tadm[26] $Yposi[27] $Tadm[27] $Yposi[28] $Tadm[28] $Yposi[29] $Tadm[29] $Yposi[30] $Tadm[30] $Yposi[31] $Tadm[31] $Yposi[32] $Tadm[32] $Yposi[33] $Tadm[33] $Yposi[34] $Tadm[34] $Yposi[35] $Tadm[35] $Yposi[36] $Tadm[36] $Yposi[37] $Tadm[37] $Yposi[38] $Tadm[38] $Yposi[39] $Tadm[39] $Yposi[40] $Tadm[40]
__________________
-- Gregory T. Gargioni ------><> E-mail: gargionis <at> gmail "dot" com ------------------------------------- |
|
September 20, 2019, 07:23 |
|
#12 | |
Senior Member
Przemek
Join Date: Jun 2011
Posts: 249
Rep Power: 16 |
Quote:
Hi How did you implement this code into CFX?
__________________
best regards pblasiak |
||
September 23, 2019, 17:09 |
|
#13 |
Senior Member
Przemek
Join Date: Jun 2011
Posts: 249
Rep Power: 16 |
Ok I found that it is in Reference guide in Power Syntax chapter
__________________
best regards pblasiak |
|
Tags |
heat transfer coefficient, wall transfer coefficien |
|
|
Similar Threads | ||||
Thread | Thread Starter | Forum | Replies | Last Post |
Natural convection in a closed domain STILL NEEDING help! | Yr0gErG | FLUENT | 4 | December 2, 2019 01:04 |
calculate heat transfer coefficient in repeated geometry | mullenc525 | CFX | 4 | January 24, 2017 15:30 |
Distribution of surface heat transfer coefficient along the axial direcion of a tube | andred | FLUENT | 0 | November 16, 2010 22:13 |
No results for solid domain | Gary Holland | CFX | 10 | March 13, 2009 04:30 |
Two-Phase Buoyant Flow Issue | Miguel Baritto | CFX | 4 | August 31, 2006 13:02 |