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December 29, 2014, 00:55 |
Condensation over tubes
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#1 |
New Member
pratik
Join Date: Jul 2014
Location: pune
Posts: 15
Rep Power: 11 |
hello friends!!!!!
I want to know,Is condensation phenomenon possible with "Evaporation-Condensation" model in Fluent??? or I must require UDF for that?? Thank you in advance!!! |
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December 29, 2014, 01:19 |
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#2 |
New Member
pratik
Join Date: Jul 2014
Location: pune
Posts: 15
Rep Power: 11 |
Hiiiiii friends!!!!!
I want to simulate condensation problem.. I have attached my mesh geometry. my problem is that i am not gettting liquid flow equal to vapour mascondensation is occuring but my liquid volume fraction at outlet is comming 4*e-10. my BCs at inlet - vapor mass flow and temperature outlet- pressure outlet Through the tubes coolant i.e. water is flowing I am using "Evaporation-condensation" model can anyone help me regarding fluent setting or any other things regarding this problem?? Any help will be greatly appreciated thank!!!! |
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December 29, 2014, 05:45 |
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#3 |
Senior Member
Paritosh Vasava
Join Date: Oct 2012
Location: Lappeenranta, Finland
Posts: 732
Rep Power: 22 |
Have you monitored the liquid volume fraction at the outlet over time? How long have you run your simulation?
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December 29, 2014, 07:01 |
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#4 |
New Member
pratik
Join Date: Jul 2014
Location: pune
Posts: 15
Rep Power: 11 |
Thank you sir for ur response!!!
I am not getting liquid at outlet but it is in all domain. I have experimental results. Experiment was carried for 322 tubes. But for simplicity I am doing simulation on 3 tubes as shown in fig. I am using mixture model, viscous laminar. In Phase interaction'Evaporation-Condensation' model sir I may be wrong in setting boundary conditions. I have given boundary conditions as follows: Inlet: vapor mass flow rate 0.00319kg/s. which was 0.3424 for 322 tubes liquid mass flow ratw 0 kg/s mixture-Temperature 313k Outlet- liquid- backflow volume fraction 1 mixture- temperature 312k tubes(convective wall)- mixture- heat flux= -2664w here i am having doubt because i have value in watt but have to give it in w/m2. which area should i take?? i have taken inside area of tube value goes very high 15485345w/m2. i have heat transfer coefficient of coolant and condensation. should i use this? inlet temp of coolant is 35.8degree cel and outlet temp of coolant is 37.4 degree cel My condensing fluid is water. please tell me How to set BCs. Thank you |
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December 29, 2014, 07:54 |
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#5 |
Senior Member
Paritosh Vasava
Join Date: Oct 2012
Location: Lappeenranta, Finland
Posts: 732
Rep Power: 22 |
Is it possible for you to send your case to me? It would be easier for me to help. My e-mail is paritoshvasava@gmail.com
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December 29, 2014, 23:58 |
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#6 |
New Member
pratik
Join Date: Jul 2014
Location: pune
Posts: 15
Rep Power: 11 |
yes, sure!!!!
i will send my case on your mail id. |
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May 29, 2018, 07:32 |
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#7 |
New Member
maofeng
Join Date: Aug 2015
Posts: 1
Rep Power: 0 |
hi bro,
have you solved this,I have the same problem,the condensation rate is very small,water volume fraction of outlet is about 10-3,and if you can give me some help, I am care about this cause it already make me crazy,Thank you。 |
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