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Naji, M. |
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Motta, Antonella |
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Aletan, Dirar |
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Mohamed, Tarek |
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Ertürk, Emre |
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Taccardi, Nicola |
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Kononenko, Denys |
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Petrov, R. H. | Madrid |
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Alshaaer, Mazen | Brussels |
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Bih, L. |
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Casati, R. |
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Muller, Hermance |
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Kočí, Jan | Prague |
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Šuljagić, Marija |
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Kalteremidou, Kalliopi-Artemi | Brussels |
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Azam, Siraj |
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Ospanova, Alyiya |
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Blanpain, Bart |
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Ali, M. A. |
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Popa, V. |
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Rančić, M. |
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Ollier, Nadège |
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Azevedo, Nuno Monteiro |
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Landes, Michael |
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Rignanese, Gian-Marco |
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Chapoy, Antonin
Heriot-Watt University
in Cooperation with on an Cooperation-Score of 37%
Topics
Publications (6/6 displayed)
- 2020Elemental Mercury Partitioning in High Pressure Fluids Part 2: Model Validations and Measurements in Multicomponent Systemscitations
- 2017Glycols Partitioning At High Pressures In Gas Processing Systems
- 2013Effect of impurities on thermophysical properties and phase behaviour of a CO2-rich system in CCScitations
- 2012An evaluation of risk of hydrate formation at the top of a pipelinecitations
- 2011Equilibrium water content in natural gas with hydrates or MEG solutions
- 2010Hydrates in High Inhibitor Concentration Systems
Places of action
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article
Effect of impurities on thermophysical properties and phase behaviour of a CO2-rich system in CCS
Abstract
CO2 captured from flue gases may contain impurities such as O2, Ar, N2 and water.The presence of such impurities in the CO2 stream can lead to challenging flow assurance and processing issues.The aim of this communication is to present experimental results on the phase behaviour and thermo-physical properties of carbon dioxide in the presence of O2, Ar, N2 and water.The effect of these impurities on density and viscosity were experimentally and theoretically investigated over the range of temperature from 243.15 K to 423.15 K up to 150 MPa.A corresponding-state viscosity model was developed to predict the viscosity of the stream and a volume corrected equation of state approach was used to calculate densities.Saturation pressures and hydrate stability (in water saturated and under-saturated conditions) of the CCS stream were also experimentally determined and modelled.This work shows that the thermodynamic models and approaches adopted were able to satisfactorily describe the thermophysical properties and phase behaviour of a typical CO2-rich stream resulting from flue gases.