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

Wall Transfer Coefficien - Heat Transfer Coefficient - CFX

Register Blogs Community New Posts Updated Threads Search

Reply
 
LinkBack Thread Tools Search this Thread Display Modes
Old   November 2, 2011, 17:49
Default Wall Transfer Coefficien - Heat Transfer Coefficient - CFX
  #1
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
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.
Gargioni is offline   Reply With Quote

Old   November 2, 2011, 20:58
Default
  #2
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
I would start by working through this FAQ:

http://www.cfd-online.com/Wiki/Ansys..._inaccurate.3F
ghorrocks is offline   Reply With Quote

Old   November 2, 2011, 22:25
Default
  #3
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
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 22:34. Reason: I forgot some things =/
Gargioni is offline   Reply With Quote

Old   November 2, 2011, 22:49
Default
  #4
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
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.
ghorrocks is offline   Reply With Quote

Old   November 2, 2011, 23:25
Default
  #5
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
"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 =]
Gargioni is offline   Reply With Quote

Old   November 2, 2011, 23:28
Default
  #6
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
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.
ghorrocks is offline   Reply With Quote

Old   November 4, 2011, 15:34
Default
  #7
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
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?
Gargioni is offline   Reply With Quote

Old   November 6, 2011, 04:57
Default
  #8
Super Moderator
 
Glenn Horrocks
Join Date: Mar 2009
Location: Sydney, Australia
Posts: 17,700
Rep Power: 143
ghorrocks is just really niceghorrocks is just really niceghorrocks is just really niceghorrocks is just really nice
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.
ghorrocks is offline   Reply With Quote

Old   March 7, 2012, 00:19
Default
  #9
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
I solved my problem... doing a CEL routine.
__________________
--
Gregory T. Gargioni ------><>
E-mail: gargionis <at> gmail "dot" com
-------------------------------------
Gargioni is offline   Reply With Quote

Old   April 15, 2013, 07:46
Default
  #10
Member
 
Join Date: Nov 2011
Location: Germany
Posts: 40
Rep Power: 14
TrII4d is on a distinguished road
maybe u can give a short summary of the steps which u made to help me?
TrII4d is offline   Reply With Quote

Old   October 24, 2017, 14:02
Default
  #11
New Member
 
Join Date: Oct 2011
Posts: 7
Rep Power: 14
Gargioni is on a distinguished road
!$Tw=298.15;
!$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
-------------------------------------
Gargioni is offline   Reply With Quote

Old   September 20, 2019, 06:23
Default
  #12
Senior Member
 
Przemek
Join Date: Jun 2011
Posts: 249
Rep Power: 15
gaza is on a distinguished road
Quote:
Originally Posted by Gargioni View Post
!$Tw=298.15;
!$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]

Hi

How did you implement this code into CFX?
__________________
best regards
pblasiak
gaza is offline   Reply With Quote

Old   September 23, 2019, 16:09
Default
  #13
Senior Member
 
Przemek
Join Date: Jun 2011
Posts: 249
Rep Power: 15
gaza is on a distinguished road
Ok I found that it is in Reference guide in Power Syntax chapter
__________________
best regards
pblasiak
gaza is offline   Reply With Quote

Reply

Tags
heat transfer coefficient, wall transfer coefficien


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
Natural convection in a closed domain STILL NEEDING help! Yr0gErG FLUENT 4 December 2, 2019 00:04
calculate heat transfer coefficient in repeated geometry mullenc525 CFX 4 January 24, 2017 14:30
Distribution of surface heat transfer coefficient along the axial direcion of a tube andred FLUENT 0 November 16, 2010 21:13
No results for solid domain Gary Holland CFX 10 March 13, 2009 03:30
Two-Phase Buoyant Flow Issue Miguel Baritto CFX 4 August 31, 2006 12:02


All times are GMT -4. The time now is 01:51.