Is contacting time a parameter for determining height of the column? What are the other parameters for determining height of the column?
In a bubble column reactor, what should be considered for calculating residence time/contacting time; Superficial velocity or velocity of the bubble at the mouth of distributer/purger?
How the flow regime changes with velocity? Is superficial velocity is a parameter for determining column diameter? Is there any rule of thumb like L/D ratio?
Does bubble size varies with surface tension of the fluid, if so how?
Please help me?
|
No replies to this topic
Share this topic:
#1
Posted 09 April 2015 - 06:47 AM
Similar Topics
Design And Fabrication Of Reflux DrumStarted by Guest_Femi_* , 22 Apr 2024 |
|
|
||
Jt Based Hcdp Design V/s Mechanical Refrigeration Hcdp Unit.Started by Guest_BabRafiq1_* , 19 Apr 2024 |
|
|
||
Diked Area Around Distillation ColumnStarted by Guest_hysyshunter_* , 15 Apr 2024 |
|
|
||
Distillation Column Decommissioning ChecklistStarted by Guest_m.bhut_* , 08 Apr 2024 |
|
|
||
Rupture Disc DesignStarted by Guest_chaupradip_* , 13 Apr 2024 |
|
|