I have a flash distillation kettle with a 16" vapor line. I am having a problem with undesired entrainment of a high boiling liquid. The kettle happens to have an agitator which hinders the typical mesh pad.
It needs to be easily removed for transitions to other products. I have seen "insertion" mist eliminators but unsure of the process of sizing these. I am not wanting to do all the sizing myself, but would like to at least do some preliminary estimations before talking to vendors.
I have several questions if someone may be able to help:
1. Has anyone ever had success in putting the mesh pad in the vapor line using a spool piece?
2. How do you calculate the required thickness of the mesh pad? (Souders-Brown to get design velocity)
3. Sizing insertion mist eliminators?
Any help would be greatly appreciated.
|

Flash Distillation Entrainment (mist Eliminators)
Started by ericflem42, Dec 03 2008 04:38 PM
2 replies to this topic
Share this topic:
#1
Posted 03 December 2008 - 04:38 PM
#2
Posted 11 December 2008 - 06:36 AM
Its not a problem where U put a mist eliminator its function & working remain same.
U can find an article on my blog also.
U can find an article on my blog also.
#3
Posted 11 December 2008 - 08:39 AM
QUOTE (pawan @ Dec 11 2008, 05:36 AM) <{POST_SNAPBACK}>
Its not a problem where U put a mist eliminator its function & working remain same.
U can find an article on my blog also.
U can find an article on my blog also.
Thanks pawan.
Similar Topics
Considering Non-Condensable Gases In DistillationStarted by Guest_riwaldron1_* , 10 Apr 2025 |
|
![]() |
||
![]() Methanol Water Distillation ColumnStarted by Guest_Kakashi-01_* , 27 Jan 2025 |
|
![]() |
||
Basic Dynamic Simulation Of A Crude Distillation UnitStarted by Guest_tomr91_* , 12 Jan 2025 |
|
![]() |
||
Kerosene Flash Point TroubleshootingStarted by Guest_zuberattan_* , 25 Oct 2009 |
|
![]()
|
||
![]() Flash Seperation For N-Butane IsomerizationStarted by Guest_CHEMICAL_LOVER_* , 04 Dec 2024 |
|
![]() |