Hi,
I'm trying to design a cryogenic air separation unit in Aspen plus. I have made the flowsheet and put all the available flow and pressure data and I have achived the desired product output along with the necessary specification. However the problem is, HP column condenser duty is not exactly same as the LP column reboiler duty. There is a difference of around 4.8 Gcal/hr. How can i improve the cold balance. Also there's an error in convergence of the recycle water stream between DCAC and waste nitrogen chill tower. Please help
Maitreyee
|

Air Separation Unit Simulation
Started by maitreyee ghosh, Apr 28 2012 05:07 AM
1 reply to this topic
Share this topic:
Similar Topics
Aspen Hysys Simulation Of Acid Gas Removal UnitStarted by Guest_R.t_* , 22 May 2025 |
|
![]() |
||
Dynamic Simulation - SeparatorsStarted by Guest_tomr91_* , 10 Mar 2025 |
|
![]() |
||
![]() Dynamic Simulation After Feed Flow ReductionStarted by Guest_Kakashi-01_* , 20 Mar 2025 |
|
![]() |
||
![]() Fixed Bed Absorber Tsa UnitStarted by Guest_Sufy_* , 13 Mar 2025 |
|
![]() |
||
![]() ![]() Molecular Sieve UnitStarted by Guest_Sufy_* , 26 Feb 2025 |
|
![]() |