AbstractDue to the continuous increase of CO2 emission to environment, the Carbon Capture and Storage (CCS) processes gained a very high importance in the last decades. One common CO2 impurity during various CCS processes is water. Therefore, the calculation of CO–water thermodynamic properties is a vital issue. This work preliminary investigates the accuracy of the extended corresponding states equation of state SPUNG using various reference fluids for the density and vapour liquid equilibrium (VLE) calculations of the CO2 - water system. The evaluation is done by comparing the numerical prediction with experimental data. The study is conducted at different mixture concentrations, and covering a broad range of conditions. The study is cond...
AbstractTransport is an important feature of the CCS process as the CO2 quality requested by pipelin...
For a good design of all the processes in Carbon Capture and Storage, the thermodynamics of the CO2 ...
It is currently acknowledged that thermodynamic models routinely used to model the behavior of fluid...
AbstractDue to the continuous increase of CO2 emission to environment, the Carbon Capture and Storag...
Due to the continuous increase of CO2 emission to environment, the Carbon Capture and Storage (CCS) ...
AbstractThe accuracy of the extended corresponding state equation SPUNG is preliminary evaluated for...
In this work, Equations of State (EoS) relevant for carbon capture and storage modelling have been e...
AbstractIn this work, Equations of State (EoS) relevant for carbon capture and storage modelling hav...
This PhD work is part of the CO2 Dynamics project in collaboration with Sintef Energy. We investigat...
The accuracy of the extended corresponding state equation SPUNG is preliminary evaluated for the den...
Precise knowledge of vapor–liquid equilibrium (VLE) data of (CO2 + diluent) mixtures is crucial in t...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
International audienceCarbon capture and storage (CCS) is nowadays considered as one of the most pro...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractTransport is an important feature of the CCS process as the CO2 quality requested by pipelin...
For a good design of all the processes in Carbon Capture and Storage, the thermodynamics of the CO2 ...
It is currently acknowledged that thermodynamic models routinely used to model the behavior of fluid...
AbstractDue to the continuous increase of CO2 emission to environment, the Carbon Capture and Storag...
Due to the continuous increase of CO2 emission to environment, the Carbon Capture and Storage (CCS) ...
AbstractThe accuracy of the extended corresponding state equation SPUNG is preliminary evaluated for...
In this work, Equations of State (EoS) relevant for carbon capture and storage modelling have been e...
AbstractIn this work, Equations of State (EoS) relevant for carbon capture and storage modelling hav...
This PhD work is part of the CO2 Dynamics project in collaboration with Sintef Energy. We investigat...
The accuracy of the extended corresponding state equation SPUNG is preliminary evaluated for the den...
Precise knowledge of vapor–liquid equilibrium (VLE) data of (CO2 + diluent) mixtures is crucial in t...
Accurate thermophysical data for the CO2-rich mixtures relevant for carbon capture, transport and st...
International audienceCarbon capture and storage (CCS) is nowadays considered as one of the most pro...
A new setup for the measurement of vapor-liquid phase equilibria of CO2-rich mixtures relevant for c...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractTransport is an important feature of the CCS process as the CO2 quality requested by pipelin...
For a good design of all the processes in Carbon Capture and Storage, the thermodynamics of the CO2 ...
It is currently acknowledged that thermodynamic models routinely used to model the behavior of fluid...