Designing a Gas Absorption Column for Ammonia
This case, the ammonia is being mixed with Air before being fed into the column. The absorbent is water that is flowing from the top.
What would happen if instead the ammonia is mixed with pure oxygen, or pure hydrogen?
Would the diffusivity affect how much ammonia is actually being removed by the water? how would we approach this problem?
|
Gas Absorption And Mass Transfer
Started by Wei, Feb 02 2009 08:08 PM
3 replies to this topic
Share this topic:
#1
Posted 02 February 2009 - 08:08 PM
#2
Posted 03 February 2009 - 07:54 AM
What will count is the binary diffusivity NH3 in O2, or H2 or whatever.
There is a direct impact on the gas side mass transfer coefficient. (the kg.a).
The kg.a is more or less proportional to the square root of the diffusivity. See ONDA's correlation for more details.
In practice, this effect is limited
There is a direct impact on the gas side mass transfer coefficient. (the kg.a).
The kg.a is more or less proportional to the square root of the diffusivity. See ONDA's correlation for more details.
In practice, this effect is limited
#3
Posted 03 February 2009 - 09:05 PM
Dear siretb Hello/ Good Morning,
Nice and heartening to see you around and helping.
Best Regards
Qalander
#4
Posted 03 February 2009 - 10:39 PM
Alright, I will look into kg,a and how it is related to the mass transfer of NH3 into O2
Thank you for the help
Thank you for the help
Similar Topics
Overall Heat Transfer CoefficientStarted by Guest_T_bag_* , 16 Apr 2024 |
|
|
||
Mass Balance ErrorStarted by Guest_Mohammad3799_* , 19 Feb 2024 |
|
|
||
Operation Of Heat Exchanger Above The Overall Heat Transfer CoefficienStarted by Guest_Papps_* , 13 Jan 2024 |
|
|
||
Solvent Carryover Emissions In Absorption ProcessStarted by Guest_TeeEng_* , 24 Oct 2023 |
|
|
||
Finding Catalyst Mass From GhsvStarted by Guest_daraj_* , 22 Sep 2023 |
|
|