Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Psv Sizing In Shell And Tube Heat Exchanger (Oil/ Water)


This topic has been archived. This means that you cannot reply to this topic.
2 replies to this topic
Share this topic:
| More

#1 Yasser M. Abd Al-Rahman

Yasser M. Abd Al-Rahman

    Brand New Member

  • Members
  • 6 posts

Posted 07 February 2017 - 04:22 PM

Dear all,

 

Regarding the PSV sizing of shell and tube heat exchanger. Hot oil in tube for heating water in shell side to steam. If I can apply relief sizing for single phase, which case I should choose; liquid or Vapor case?

 

Thanks a lot



#2 shahidulislam48

shahidulislam48

    Gold Member

  • Members
  • 104 posts

Posted 08 February 2017 - 11:36 PM

Hi,

 

It depends on which side you are willing to put your PSV.

 

You had better try these links to have a preliminary idea.

 

http://www.cheresour...heat-exchanger/

http://www.cheresour...-for-fire-case/

http://www.cheresour...-for-exchanger/

http://www.cheresour...f-an-exchanger/


Edited by shahidulislam48, 08 February 2017 - 11:39 PM.


#3 paulhorth

paulhorth

    Gold Member

  • ChE Plus Subscriber
  • 396 posts

Posted 23 February 2017 - 02:23 PM

Yasser.

 

if I understand you correctly, you have a steam boiler heated by hot oil.  The steam side has to be protected by a relief valve. The relieved fluid is steam. (just like on an old fashioned railway loco). There are several relief cases. The blocked outlet case relief rate is the maximum steam generation rate at the relief pressure and with normal hot oil flowrate.  You should also check the case with maximum hot oil flow (hot oil control valve failure case). In this case you can take credit for the normal process steam flow continuing, the extra steam has to be relieved.  Another case would be tube rupture, if the hot oil pressure is higher than the steam side pressure, hot oil flowing directly into the water will generate a lot of steam.

The hot oil side will need a relief valve if its design pressure is lower than the steam side design pressure.

 

Paul






Similar Topics