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September 10, 2014, 10:30 |
Boundary condition of velocity inlet
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#1 |
Member
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13 |
hello guys
i simulate shell&tube heat exchanger in fluent. i use velocity inlet boundary condition. now i question that i must select which options in turbulence part of velocity inlet boundary condition? K and ep. intensify and length scale. intensify and velocity ratio. intensify and hydraulic diameter.
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September 13, 2014, 01:42 |
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#2 |
Senior Member
A-A Azarafza
Join Date: Jan 2013
Posts: 226
Rep Power: 14 |
It depends on your problem and inlet geometry but in most cases, the third option is more straightforward.
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September 13, 2014, 02:43 |
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#3 |
Member
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
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tanks about your Ans.
I don't know why mass flow rate at inlet and outlet not be equal?! this heat exchanger has two fluid domain (Water&Oil). water: inlet - velocity inlet outlet - pressure outlet -------------------------- Oil: inlet - velocity inlet outlet - pressure outlet ------------------------------- That this domains are coupled(Thermal condition) together. for example mass flow rate at inlet and outlet : water inlet= 1.132 water outlet=0.746 oil inlet=0.171 oil outlet=0.521
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September 13, 2014, 15:28 |
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#4 |
Member
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
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Use intensity and hyd. dia bc. option...you can find empirical relations for I and D involving velocity and geometry data in fluent user guide....just looking at those mass flow rates gives me the impression that water is entering into oil flow domain...some sort of leakage...please check your geometry construction ..... Good luck!
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September 14, 2014, 02:45 |
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#5 |
Member
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13 |
tanks about your ans.
my geometry is ok. i think my mesh file is not suitable.but i cant improve mesh file. its very complex.if possible i send ansys file(project-workbench) for you that you check it.email address please?
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September 14, 2014, 03:03 |
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#6 |
Member
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 13 |
vdp6786@hotmail.com.... I'll have a look
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September 14, 2014, 11:16 |
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#7 |
Member
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13 |
i send project file for you .
thanks about your att.
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September 15, 2014, 11:57 |
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#8 |
Member
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 13 |
Hi....i got the file but unfortunately your ansys is newer so files couldn't be supported by my system...is there any way around?
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September 15, 2014, 13:44 |
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#9 |
Member
Sa.Baraty
Join Date: Apr 2013
Location: Iran
Posts: 50
Rep Power: 13 |
Thanks. i sent 'stp' file of my model for you
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September 18, 2014, 21:14 |
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#10 |
Member
Virendrasingh Pawar
Join Date: Jun 2013
Posts: 47
Rep Power: 13 |
Hi...i got the geometry....just one doubt...the end where the tube-side fluid (i guess oil in your case) reverses (the semi-sphere at top end)....shouldn't there be plates installed...or else shell-side fluid (water) will intermix...please clear
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