Hello, I've simulated a process in HYSYS, with several columns, one of which is a deethanizer modelled as a reboiled absorber. I'm trying to perform hand calculations to see whether I obtain the same number of trays as HYSYS. I need to absorb propene and heavier from the gas stream.
1. However, it is a multicomponent system, so I am having dificulty obtaining the equilibrium data from HYSYS (my teacher said that I can obtain the equilibrium curve from HYSYS). How do I do this please? (It contains methane all the way to decane). I don't mind whether it is the Temperature/compostion equilibrium graph as I can then obtain x & y myself and plot it, however, I am completely lost as to how to do this with a multicomponent system on HYSYS. I really need the equilibrium curve graph so that I can then plot the operating line and obtain the equilibrium number of trays requird.
2. Also, my gas stream is concentrated, so how do I calulate the value of A (absorption factor) and K, as my liquid and gas flowrates are not constant? I tried obtaining K values myseld from the DePriester charts, and they were very similar to the values produced by HYSYS, and the temperature varies significantly down the column.
Thankyou in advance.
|

Vle In Hysys
Started by Guest_RCW_*, Feb 11 2010 02:35 PM
No replies to this topic
Share this topic:
#1
Guest_RCW_*
Posted 11 February 2010 - 02:35 PM
Similar Topics
Aspen Hysys Simulation Of Acid Gas Removal UnitStarted by Guest_R.t_* , 22 May 2025 |
|
![]() |
||
![]() Hysys Expander/compressor Input Using Dimensionless CurveStarted by Guest_Alfreedo_* , 21 Apr 2025 |
|
![]() |
||
Water Hammer Study: Hysys Dynamics Vs PipenetStarted by Guest_powerox29_* , 07 Apr 2025 |
|
![]() |
||
Need Help In Hysys For Production Of Vinyl AcetateStarted by Guest_christinalee12_* , 31 Mar 2025 |
|
![]() |
||
Aspen Hysys - Blowdown Utility Heat Flux MethodStarted by Guest_yuvi.ardekar1999@gmail.com_* , 27 Feb 2025 |
|
![]() |