Continue to Site

Eng-Tips is the largest engineering community on the Internet

Intelligent Work Forums for Engineering Professionals

  • Congratulations cowski on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

Blowdown with liquids

Status
Not open for further replies.

Renoyd

Mechanical
Feb 11, 2007
41
Hello,
For gas plant blowdown calculation, if the vessel has liquid in it, how would the calculation be done?

Thanks
 
Replies continue below

Recommended for you

as for gases but take care to
liquids have higher densities than gases which means higher forces in velocity changes (by momentum conservation)
liquids can vaporize, the cool down process can produce temperatures which are below the limits admitted for the plant's materials
 
Hopefully, your liquid will remain in the blowdown vessel. If you don't have a dynamic simulator then run successive flashes at about 1-2 minutes interval. You should be trying to reduce pressure by half in 15 minutes. Calculate the mass removed during the interval, recalculate the liquid composition, then reflash. With LPG you should see the temp drop.
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor