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

0

Relief Valve Sizing


2 replies to this topic
Share this topic:
| More

#1 sau1a86

sau1a86

    Brand New Member

  • Members
  • 3 posts

Posted 14 September 2020 - 02:14 AM

Can anyone please help me with the basics of how to go about a Relief valve sizing ? any solved examples would also do  



#2 breizh

breizh

    Gold Member

  • Admin
  • 6,347 posts

Posted 14 September 2020 - 02:32 AM

Hi,

Download the engineering document using this link . You will find a bunch of good information about sizing , more important is to define the scenario requiring the PSV :

https://www.leser.co...ls/engineering/

 

To me you need to consult knowledgeable people , senior peers among your organization .

Good luck

Breizh 


Edited by breizh, 14 September 2020 - 03:51 AM.


#3 Subhendu

Subhendu

    Brand New Member

  • Members
  • 8 posts

Posted 30 September 2020 - 04:48 AM

Hi,

 

Pressure relief sizing is a vast subject, and is very difficult to capture the same in a post. To size a relief valve you need to follow the below steps

  1. Firstly, you need to identify all plausible causes of overpressure, that may or may not have a relief load. For list of possible causes of overpressure please refer to API Std 521. Afterwards, you have to calculate the relief loads associated with each possible cases.
  2. Next refer to API Std 520 Part 1, where different sizing equations are provided for liquid relief, vapor relief or two-phase relief. Based on these equations you will be able to calculate the required orifice area corresponding to each relief case.
  3. Next refer to API Std 526 for selection of orifice letter (D having the smallest and T having the largest orifice area) based on required orifice area. However, please note that orifice letter thus selected can vary from the PSV vendor recommendation because of the difference in various constants used in the sizing equations. 

Also, please be advised that type of PSV also affects the design. As a general rule of thumb, if backpressure is less than 10% of PSV set pressure, you can use conventional PSV, unless there is significant variation in the superimposed backpressure, > 3%, in that case balanced bellow valves are to be used.

If difference between the operating pressure and design pressure is less than 10%, then you need to use a Pilot type PSV.






Similar Topics