Hello all,
I am needed to perform adequacy checks for a tray distillation column. The new operation will result in lower vapor loads as the feed is heavier in nature, so I wish to check adequacy during turndown.
I have used KG tower but, it gives only one paramter that is Turndown% which is equivament to % of valves to be open during turndown mode.
Is there any other software that examines the turndown and gives result in more detalied way, such as Downcomer sealing etc...
Thansk for your help in advance....
alok
|

Tray Adequacy Checks For Turndown Operation
Started by B-2 Spirit, Feb 03 2012 06:27 AM
tray adequacy for turndown
4 replies to this topic
Share this topic:
#1
Posted 03 February 2012 - 06:27 AM
#2
Posted 04 February 2012 - 07:41 AM
Hi Alok,
I have seen in KG tower result details about weeping check is not in much details.
I am using sultech package for hydraulics(Internal version of sulzer).
For customer version there is sulcol package available on Sulzer site, below is the link:
http://www.sulzerche...aspx/tabid-199/
For this you have to apply for it, sulcol have more details than KG tower, it show VSF/VSFmin which should above certail value to avoid weeping at low rates..
Apart from this you can check manually also:
At low vapor rate there will be liquid passing through holes. Hole area to be selected such that vapor velocity at lower operating point will be above the weep point.
Minimum vapor velocity is given by:
uh=(K2 - 0.9(25.4-dh))/(DenV)^0.5
K2 is contant depends on depth of clear liquid on plate. Find attached graph..
which will be hw-hight of weir + how hight over wier.
how = 750 *(Lw/(denL*lw))^(2/3)
Lw-Liquid flow rate(kg/sec)
lw-wier length (m)
how- wier crest (hight above wier) mm
for even flow of liquid over plate how should be atleast 10mm
Vapor velocity through the hole should be higher than uh to avoid weeping..
I hope this will be helpful...
Regards,
Abdul Rashid
I have seen in KG tower result details about weeping check is not in much details.
I am using sultech package for hydraulics(Internal version of sulzer).
For customer version there is sulcol package available on Sulzer site, below is the link:
http://www.sulzerche...aspx/tabid-199/
For this you have to apply for it, sulcol have more details than KG tower, it show VSF/VSFmin which should above certail value to avoid weeping at low rates..
Apart from this you can check manually also:
At low vapor rate there will be liquid passing through holes. Hole area to be selected such that vapor velocity at lower operating point will be above the weep point.
Minimum vapor velocity is given by:
uh=(K2 - 0.9(25.4-dh))/(DenV)^0.5
K2 is contant depends on depth of clear liquid on plate. Find attached graph..
which will be hw-hight of weir + how hight over wier.
how = 750 *(Lw/(denL*lw))^(2/3)
Lw-Liquid flow rate(kg/sec)
lw-wier length (m)
how- wier crest (hight above wier) mm
for even flow of liquid over plate how should be atleast 10mm
Vapor velocity through the hole should be higher than uh to avoid weeping..
I hope this will be helpful...
Regards,
Abdul Rashid
Attached Files
#3
Posted 06 February 2012 - 09:00 AM
thanks bro.
have applied for sulcol but no reply, however, i will definitely chk for your manual calculations.
thanks again
have applied for sulcol but no reply, however, i will definitely chk for your manual calculations.
thanks again
#4
Posted 07 February 2012 - 04:45 AM
Hello Abdul,
I noticed that the formulae you gave applicable for sieve trays, I am handling moveable valves. Do we have any correlations for checking weeping in moveable valve trays.
regards,
Alok
I noticed that the formulae you gave applicable for sieve trays, I am handling moveable valves. Do we have any correlations for checking weeping in moveable valve trays.
regards,
Alok
#5
Posted 14 February 2012 - 10:22 AM
There is no weeping in the moveable valve trays.
Similar Topics
Petrosim Tray SizingStarted by Guest_tomr91_* , 27 Feb 2025 |
|
![]() |
||
![]() Strategy For Adequacy Check Of Multiple Bdvs In A SystemStarted by Guest_nabeelsp1036_* , 22 Jan 2025 |
|
![]() |
||
Uniform Vs Non-Unfiorm Tray In HysysStarted by Guest_tomr91_* , 23 Jan 2025 |
|
![]() |
||
Chimney TrayStarted by Guest_tomr91_* , 20 Jan 2025 |
|
![]() |
||
![]() How Is The Performance Of The Distillation Tray Calculated? The DistanStarted by Guest_Ahmedforup_* , 11 Oct 2024 |
|
![]() |