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

2

Thermal Relief Valve For A Fire Case

trv thermal relief fire case fire

2 replies to this topic
Share this topic:
| More

#1 QuantumEng

QuantumEng

    Brand New Member

  • Members
  • 8 posts

Posted Yesterday, 01:53 PM

Hello all,

 

Would the installation of a typical 3/4"x1" TRV on the shell side of a S&T heat exchanger be acceptable for a fire case scenario?

1. The relieving fluid is liquid lube oil, not expected to vaporize, only expand, so there is no need for a vapor trim.

2. The required relieving capacity is about 2 gpm, well within the capacity of a typical size TRV.

 

The true scenario would technically be relief due to thermal expansion, however, the thermal expansion would only happen due to a sustained pool fire. For context, the exchanger is a lube oil cooler, so there would be no abnormal heat input on any other case. 

 

Base on my reasoning mentioned above, I do not see a reason for a TRV to not work, however, is there any sections within API or ASME that would advice against this? Alternatively, the required PSV would be a 1D2, which seems like overkill all things considered.

 

 

Thanks in advance.


Edited by QuantumEng, Yesterday, 02:16 PM.


#2 breizh

breizh

    Gold Member

  • Admin
  • 6,854 posts

Posted Yesterday, 09:10 PM

Hi,

You may find pointers in the doc attached.

Breizh



#3 fallah

fallah

    Gold Member

  • ChE Plus Subscriber
  • 5,026 posts

Posted Yesterday, 10:25 PM

Hello all,

 

Would the installation of a typical 3/4"x1" TRV on the shell side of a S&T heat exchanger be acceptable for a fire case scenario?

1. The relieving fluid is liquid lube oil, not expected to vaporize, only expand, so there is no need for a vapor trim.

2. The required relieving capacity is about 2 gpm, well within the capacity of a typical size TRV.

 

The true scenario would technically be relief due to thermal expansion, however, the thermal expansion would only happen due to a sustained pool fire. For context, the exchanger is a lube oil cooler, so there would be no abnormal heat input on any other case. 

 

Base on my reasoning mentioned above, I do not see a reason for a TRV to not work, however, is there any sections within API or ASME that would advice against this? Alternatively, the required PSV would be a 1D2, which seems like overkill all things considered.

 

 

Thanks in advance.

 

In general, because the required capacity is within the capacity of typical size of TRV there would be no problem using mentioned TRV for fire case of such liquid filled shell of a shell and tube heat exchanger otherwise the pool fire would be so sustained that leading to lube oil vaporization when the exchanger has been isolated and might need to be depressurized before reaching the TRV to the prespecified set point.


Edited by fallah, Yesterday, 10:26 PM.





Similar Topics