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Shell And Tube Heat Exchanger Simulation


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#1 kylene28

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Posted 09 May 2008 - 05:46 AM

I want to try simulating a shell and tube heat exchanger using aspen. What are the parameters needed to start the simulation? Please advise me regarding this.

#2 riven

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Posted 09 May 2008 - 06:44 AM

The exact same parametrs you need to design it by hand.

Have you even sat in front of the aspen control? It asks for all the inputs right in front of you.

#3 kylene28

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Posted 09 May 2008 - 10:54 PM

Thanks for your reply. Previously I go through heat exchanger simulation with no phase change using the basic heat exchanger calculation. Can I use the same for shell and tube heat exchanger?

#4 phoenixtree

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Posted 11 May 2008 - 07:11 AM

Use Aspen HTFS to do the simulation.

#5

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Posted 14 May 2008 - 10:59 PM

Dear all,

I was trying to size the shell and tube heat exchanger for condensation service. On the shell side i have mixture of light alcohols and on tube side cooling water. I tried to rate exchanger in simulators, and heat exchanger softwares which are available commercially but what i observed is interesting.
The overall heat transfer coefficient for vertical and Horizontal condenser was almost equivalent, which should not be a case.
Can anybody tell me that whether i am doing a mistake or this is a problem or a bug in these softwares.
Cheers!! blink.gif blink.gif

#6 raajesh

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Posted 25 July 2008 - 10:06 AM

Sir

I want to study some tutorials on HTFS for heat exchanger simulation. Can u provide me any link to download HTFS tutorials...

Thank you

#7 Zauberberg

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Posted 25 July 2008 - 11:00 AM

This one is still available online: http://www.nioc.org/...asc/tasc_gs.pdf

#8 Jenergy

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Posted 10 September 2010 - 03:58 AM

Dear all,

I was trying to size the shell and tube heat exchanger for condensation service. On the shell side i have mixture of light alcohols and on tube side cooling water. I tried to rate exchanger in simulators, and heat exchanger softwares which are available commercially but what i observed is interesting.
The overall heat transfer coefficient for vertical and Horizontal condenser was almost equivalent, which should not be a case.
Can anybody tell me that whether i am doing a mistake or this is a problem or a bug in these softwares.
Cheers!! Posted Image Posted Image


I have a sentence in PERRY's CHEMICAL ENGINEERS' HANDBOOK seems related to it;
"At high condensing loads, with vapor shear dominating, tube orientation has no effect, and..."(5-22 page)

#9 Padmakar Katre

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Posted 13 September 2010 - 09:00 AM

This one is still available online: <a href="http://www.nioc.org/...sc/tasc_gs.pdf" target="_blank">http://www.nioc.org/...tasc_gs.pdf</a>

Dear Zauberberg,
Could you please recheck the link as it doesn't work with me. Thanks in advance and have a nice time there.




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