MedFidelityArtist
Chemical
- Oct 17, 2007
- 2
Hi,
I am charged with doing a medium fidelity simultion of a gas/oil/water seperator. It is controlled at 50psig with a water interface LIC for the bottom water and a weir over which the oil flows when over a particular level.
I have it modelled somewhat as I would expect it to act in real life. I know the oil and water flowrates in. The retention time I am saying is the holdup in MBD divided by the (water + oil flowrates out). How would I model this though for intial startup as retention time would be infinity with no flow rates out but holdup increasing (thus producing immediate and full seperation which isn't correct I presume). It would seemingly work for the steady state condition.
Also, what if the vessel was inventoried already with a fully seperated volume of water and oil.
Any help would be appreciated!
Thanks,
Greg
I am charged with doing a medium fidelity simultion of a gas/oil/water seperator. It is controlled at 50psig with a water interface LIC for the bottom water and a weir over which the oil flows when over a particular level.
I have it modelled somewhat as I would expect it to act in real life. I know the oil and water flowrates in. The retention time I am saying is the holdup in MBD divided by the (water + oil flowrates out). How would I model this though for intial startup as retention time would be infinity with no flow rates out but holdup increasing (thus producing immediate and full seperation which isn't correct I presume). It would seemingly work for the steady state condition.
Also, what if the vessel was inventoried already with a fully seperated volume of water and oil.
Any help would be appreciated!
Thanks,
Greg