|
|
0
Brand New Member
Posted 30 October 2019 - 08:11 PM
I'm trying to find out when a simple water/hydrogen cooling tower packed with 2" pall rings will begin to flood. I've worked out the superficial gas velocity and the liquid loading velocity, i've also found the void fraction/packing factor etc. but i can't find any data/graphs with regards to flood points. Is there a way i can calculate this without needing graphs?
Kind regards
Gold Member
Posted 31 October 2019 - 12:08 AM Best Answer
Hi ,
Consider the resource attached.
Other resource : Perry's chemical engineers' handbook
Good luck
Breizh
Diked Area Around Distillation ColumnStarted by Guest_hysyshunter_* , 15 Apr 2024 |
|
|
||
Distillation Column Decommissioning ChecklistStarted by Guest_m.bhut_* , 08 Apr 2024 |
|
|
||
Hydrocarbon Dew Point Control UnitStarted by Guest_BabRafiq1_* , 05 Apr 2024 |
|
|
||
Distillation Column DiameterStarted by Guest_refluxraider_* , 12 Mar 2024 |
|
|
||
Diameters Of A Structured Packing Distillation Column With No VapourStarted by Guest_hysyshunter_* , 07 Mar 2024 |
|
|
Forums
Blogs
Articles
File Library
FAQ
Search
FB
