jhamil1
Mechanical
- Oct 28, 2008
- 18
All,
I have been using GCAP8.2 equation of state software to develop phase diagrams to determine if liquids are dropping out of a natural gas stream. The gas composition has been entered into the software and a phase diagram is produced. It also produces two additional curves for hydrate dew point and water dew point with respect to temperature and pressure. Here is a link of what I am talking about
I don't know if any one has used this program or if it is a good program. I do not do this on a regular basis and I need some clarification. I know the circondentherm temperature is the point at which liquids will begin to drop out. I have this information from the chromatograph data. What I don't understand about the GCAP software is the hydrate dew point curve is above this point.
+ Will hydrates of heavier hydrocarbons drop out before the circondentherm temperature is reached?
I have been using GCAP8.2 equation of state software to develop phase diagrams to determine if liquids are dropping out of a natural gas stream. The gas composition has been entered into the software and a phase diagram is produced. It also produces two additional curves for hydrate dew point and water dew point with respect to temperature and pressure. Here is a link of what I am talking about
I don't know if any one has used this program or if it is a good program. I do not do this on a regular basis and I need some clarification. I know the circondentherm temperature is the point at which liquids will begin to drop out. I have this information from the chromatograph data. What I don't understand about the GCAP software is the hydrate dew point curve is above this point.
+ Will hydrates of heavier hydrocarbons drop out before the circondentherm temperature is reached?