WHY THE HEAT EXCHANGER SIMULATION APPEAR FLASH FAILURE CALCULATION WHEN I PUT THE SHELL SIDE PARAMETER (H2O) INLET temperature 42 and 80 and tube side gas (co2) inlet temp. 97 and calculate out let appear flash failure calculation...where the problem plz
|
|
Flash Failure In Calculation In Heat Exchanger Hysys
Started by AHMEDENAS3385, Jun 25 2021 05:52 PM
1 reply to this topic
Share this topic:
#1
Posted 25 June 2021 - 05:52 PM
#2
Posted 25 June 2021 - 06:07 PM
By setting the water side temperature difference and flow rate, you are also fixing a duty for the exchanger. I suspect when you apply that duty to the gas side, the resulting gas condition would be unrealistic. The simulation cannot supply a converged answer for the conditions you supplied.
Similar Topics
Selection Of Heat Exchanger For Heating LiquidStarted by Guest_fahctory_* , 24 Feb 2026 |
|
|
||
How To Estimate The Water Dewpoint From Heat And Mass Balance Of NaturStarted by Guest_krishnnaa26_* , 30 Apr 2026 |
|
|
||
Importing Component Stream Data From Hysys To Excel Using VbaStarted by Guest_TimL_* , 17 Aug 2018 |
|
|
||
The Basis Of Calculation To 3% Pressure Loss At The Inlet Of PressureStarted by Guest_phoenixmoca_* , 14 Mar 2026 |
|
|
||
Heat Exchanger Temperature CrossStarted by Guest_kaidlut_* , 20 Dec 2022 |
|
|

FB





