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

Flare Stack Rating Consideration


This topic has been archived.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

#1 kloroform

kloroform

    Brand New Member

  • Members
  • 6 posts

Posted 12 June 2015 - 02:43 AM

dear all,

i need to evaluate the flare stack performanceicon1.png, the existing flare is designed to dispose around 50 MMSCFD natural gas , due to demand increasement from buyer, the flare shall be capable to handle 65 MMSCFD disposal gas (block discharge scenario governs the flow rate)
i have some questions regarding this flare rating :

a. Flare Mach Number :
as per API RP 521, mach number in flare tip shall be 0,5 at emergency scenario. based on the condition at 65 MMSCFD, the mach number is 0,7 for the existing diameter of flare. what will happen if the mach number is 0,7 ? what is the negative effect ?

b. Flare Velocity :
according to API RP 521, there is phenomenon called blowoff (high flare velocity) or flashback (low flare tip velocity). since there is increasement in flowrate ( up to 65 MMSCFD), blowoff may happen in the flare stack. the problem is... i can't find the velicity limit to avoid blowoff (or flashback) in API RP 521
could you please point me out in what paragraph that this limit available in API RP 521 ? (or other references)

c. Noise Limit
due to higher velocity, excessive noise may become a problem, again, i can't find the noise limit for flare in API RP 521. could you please point me out in what paragraph that this limit available in API RP 521 ? (or other references)


d. additional flare
is it ok to just add another flare in a flare system networkicon1.png ? i mean, since the existing flare is 50 MMSCFD, i am considering to buy another flare with 15 MMSCFD (50+15 = 65 MMSCFD). what should i consider for this option ? or is it better if i just buy one flare in 65 MMSCFD capcacity ? i don't think back pressure in PRV will be a problem since only one flare header available


My reference : API RP 521, 1997 edition.



thanks in advance, i really need your help.
 

 



#2 shan

shan

    Gold Member

  • ChE Plus Subscriber
  • 692 posts

Posted 12 June 2015 - 07:31 AM

a.  Replace you flare tip.  There are sonic flare tips and supersonic flare tips on the market.

b.  See a.

c.  80 dB(A) at plant fence per EPA.

d.  See a.  



#3 mosayef

mosayef

    Veteran Member

  • Members
  • 33 posts

Posted 12 June 2015 - 08:30 PM

why should i replace my flare tip ? could you place elaborate more, shan ?  the maximum mach number is below 1 (0,7). so it is subsonic. why should i choose sonic tip Flare ?

 

thanks :)


Edited by mosayef, 12 June 2015 - 08:39 PM.


#4 shan

shan

    Gold Member

  • ChE Plus Subscriber
  • 692 posts

Posted 17 June 2015 - 02:57 PM

As indicated in API Standard 521 (2007) Page 76:"Experience has shown that a properly designed and applied flare burner can have exit velocity of more than March 0.5, if pressure drop, noise and other factors permit."  Not as what you mentioned "as per API RP 521, Mach number shall be 0.5 at emergency scenario".






Similar Topics