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Block Bypass Streams In Htri


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#1 krsna

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Posted 27 December 2012 - 02:33 AM

What is the significance of A, E, F Streams in HTRI

#2 Pilesar

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Posted 27 December 2012 - 01:29 PM

You can find a good explanation at the link below:
http://www.wlv.com/p...data/db3ch3.pdf

#3 himant

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Posted 16 July 2013 - 10:49 AM

Hi

 

I have a doubt regarding stream analysis.

I designed a exchanger using HTRI and it shows B flow as 0.4, C as 0.3, A as 0.2 and E as 0.1.

 

And if I block A and E streams, my heat transfer comes out to be same as case with no block flows.

 

So, will my exchanger work with lesser B flow? And what is the significance of stream analysis if my exchanger is giving desired outlet with lesser area?

 

Regards

Himant



#4 Pilesar

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Posted 16 July 2013 - 01:19 PM

If you are using HTRI in design mode, the heat transfer will be the same for every configuration. When you specify the inlet and outlet conditions of one of the streams, there are no degrees of freedom to adjust the overall duty. Are you running HTRI in design mode? To address your specific questions, for exchangers where the tube side coefficient greatly dominates the total thermal resistance the flow path on the shell side will not significantly affect performance -- condensers are often a good example.



#5 himant

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Posted 16 July 2013 - 10:40 PM

Thank you for your reply.

 

I was running HTRI in design mode. To be more clear about my case, I am attaching screenshot of my case.

I have just used water in shell and tube. Area comes out to be around 77 m2.

 

In this case, there is not dominance from shell side and tube side. Main problem is with the stream analysis and window and cross-flow velocities.

 

At this moment, I am not concerned about vibrations.

 

Regards

Himant

 



#6 himant

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Posted 16 July 2013 - 10:43 PM

Attached file

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