Hi,
I'd like to know if SS316L is suitable for use for a distillation column bottom given following conditions:
Inlet Flow (tower middle) - 712 Kg/hr at
* Temperature - 85 degC ,
* Process Stream Composition - water 56%, Methanol 19.9%, Glycerol 21.8%, NaCl 1.2%, Fatty Matter 1.1%.
Outlet flow (tower bottom) - 594.93 Kg/hr at
* Temperature - 105 degC.
* Process Stream composition - water 69.9%, Methanol 0.1%, Glycerol 27.2%, NaCl 1.5%, Fatty Matter 1.3%.
Ph of inlet and bottom outlet streams is 6-7.
Possible Corrosive matter : Chlorides and fatty matter( fatty acids)
Thanks in advance.
|

Selection Of Moc For Tower Bottom
Started by onyxgaze, Mar 15 2006 05:20 AM
1 reply to this topic
Share this topic:
Similar Topics
![]() Steam Carrying Liquid From The Sour Water Stripping TowerStarted by Guest_kaidlut_* , 12 Sep 2024 |
|
![]() |
||
![]() Distillation Column Top & Bottom TemperaturesStarted by Guest_halkeshhulk_* , 09 Jun 2025 |
|
![]() |
||
![]() Distillation Tower Top And Bottom Temperature And PressureStarted by Guest_student55_* , 27 Mar 2016 |
|
![]()
|
||
Selection Type Of Heater For Refrigerated PropaneStarted by Guest_livetolove003_* , 07 May 2025 |
|
![]() |
||
![]() Activated Carbon SelectionStarted by Guest_Talhafarooq_* , 25 Nov 2024 |
|
![]() |