Just today I saw an example of how not to specify te elevation of equipment. A couple of years ago I saw another example of this and on both occasions HYSYS was blamed to produce the wrong results.
The relative elevation of the nozzles should ALWAYS be set as the are in reality. Do NOT use this relative elevation as a fudge for the total elevation! For example, you don't tell HYSYS that the base elevation of a valve is zero meters and then set the nozzle elevations of inlet and outlet to 12 meters to tell HYSYS that the valve is really located at an elevation of 12 meters.
The risk you run is wrong results. One of the causes of this is that HYSYS will do it's flash clculation at a pressure that corresponds with base elevation of the equipment. So if your valve carries a vapour that is close to the dew point and it comes out of tall equipment (a column for example), the flash calculation may get done at a pressure that is noticeably higher thant the column pressure and hence show some lquid drop out which isn't there in reality.
Wednesday, 9 January 2008
How NOT to specify equipment elevation in dynamic modelling
Posted by
Kwizim
at
21:17
Labels: Dynamic, Elevation, Static Head
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Contents By Category
Utility
Dynamic
- Did You Know Series: Manipulating flows in dynamics
- Dynamic Modelling of Flare Networks
- The HYSYS Process Data Tables - The Ugly Duckling
- Modelling Valves in HYSYS Steady State and Dynamics
- Modelling process piping in HYSYS Dynamics
- Use the HYSYS Carry-over capability to unclutter your PFD
- How NOT to specify equipment elevation in dynamic modelling
Steady State
- Did you know series: You can set a component ratio using the balance block
- The HYSYS Process Data Tables - The Ugly Duckling
- Modelling Valves in HYSYS Steady State and Dynamics
- What does "Compressible Flow" mean? Isn't any gas compressible?
- Using Electrolytes in HYSYS - Some things are good to know
- My column initially converges, but with a different feed it fails to converge
- Causes of inconsistencies can be elusive
- Make sure you have an understanding of the complete process when modelling
- Use the HYSYS Carry-over capability to unclutter your PFD
- Don't blame the simulator, at least not right away
- Matching the oil density from PVT analysis with HYSYS results
- Depressuring studies and the HYSYS depressuring utility
- The HYSYS column solver may be able to do more than you think
Thermodynamics
- Did you know series: When using Lee-Kesler Enthalpies with the PR EOS, you get better enthalpies AND ASME steam enthalpies for water as a bonus
- Using Electrolytes in HYSYS
- Using Electrolytes in HYSYS - Some things are good to know
- Modelling TEG Dehydration accurately
- Dealing with thermodynamics: the difference between petroleum industry and chemical industry
- Matching the oil density from PVT analysis with HYSYS results
1 comment:
Yes, when we specified this model, we made this error. It only came to light however, because we were working on the simulation in two different versions. Hysys 2004.2 patch 0 returned a pressure drop higher than our manual test calculation, while Hysys 2004.2 patch 5 returned an impossible negative pressure drop for flow througn the same pipe segment. We forwarded the model to Aspentech for advice, who replied that version 2004.2 patch 0 was flawed and should not be used for this model. They did not notice our error in specifying the elevations. This was not detected until the blogger himself reviewed our model. The model now works correctly , but not in version 2004.2 patch 0. With the elevations correctly specified, the patch 5 version calculates pressure drops in line with our manual calculation, and we are now satisfied that we have a working model.
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