EmmanuelTop
Chemical
- Sep 28, 2006
- 1,237
When calculating hydrate formation conditions for a given process stream, knowing its pressure and composition, Aspen software output defines a “hydrate formation temperature” – which is a fixed value for that particular pressure and composition.
Searching through literature resources, I found that for each operating pressure only one temperature corresponds to the hydrate formation point.
1. If process stream is flowing at temperatures that are below hydrate formation temperature, will hydrate formation occur?
2. If two- or three-phase fluid is involved in hydrate formation study, which hydrate prediction model should be used? Usually there are “Symmetric”, “Asymmetric”, “Vapor only” or “Free water present” correlation models. The use of these predictive models is based not on the number of phases present in the system, but on the phase that is in equilibrium with hydrate solids. How to establish which is the correct equilibrium model, since each of these comes with a different hydrate temperature as calculation output?
3. When developing a P-T hydrate curve for a given stream, is there any way to switch between different hydrate prediction models within the P-T envelope – since the fluid may exist as single phase (vapor), two-phase (vapor + hydrocarbon liquid) or three-phase (vapor + hydrocarbon liquid + aqueous phase) system, or it has to be done manually?
Thanks in advance,
Searching through literature resources, I found that for each operating pressure only one temperature corresponds to the hydrate formation point.
1. If process stream is flowing at temperatures that are below hydrate formation temperature, will hydrate formation occur?
2. If two- or three-phase fluid is involved in hydrate formation study, which hydrate prediction model should be used? Usually there are “Symmetric”, “Asymmetric”, “Vapor only” or “Free water present” correlation models. The use of these predictive models is based not on the number of phases present in the system, but on the phase that is in equilibrium with hydrate solids. How to establish which is the correct equilibrium model, since each of these comes with a different hydrate temperature as calculation output?
3. When developing a P-T hydrate curve for a given stream, is there any way to switch between different hydrate prediction models within the P-T envelope – since the fluid may exist as single phase (vapor), two-phase (vapor + hydrocarbon liquid) or three-phase (vapor + hydrocarbon liquid + aqueous phase) system, or it has to be done manually?
Thanks in advance,