AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline simulator to data obtained using the multi-stage (MUSTA) centred scheme. The case considered is a depressurization of a pipeline. Care was taken to compare the same flow model and thermodynamic equation of state. The two methods appear to converge on fine grids, but on coarse grids, the MUSTA method is more accurate
AbstractThe objective of the present study is to gain an understanding on the effect of impurities d...
Pressurized liquefied gases such as carbon dioxide are transported at a pressure above their saturat...
Key to the transport phase of carbon capture and storage (CCS) is understanding the behavior of liqu...
A numerical benchmark study has been performed, comparing results from the OLGA pipeline simulator t...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
AbstractA model for two-phase carbon dioxide transport with phase transfer in pipelines is presented...
A model for two-phase carbon dioxide transport with phase transfer in pipelines is presented. The st...
AbstractWe describe the results of depressurizing an onshore 50km long, 24 inches buried pipeline fr...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractThe present paper concerns the importance of a combined modelling and experimental effort to...
AbstractPressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen ha...
Pressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen have been ...
In this work the Schlumberger flow assurance tool OLGA and SINTEF Energy Research in-house CFD tool ...
AbstractThe development, testing and validation of a two-fluid transient flow model for simulating o...
AbstractAccurate knowledge and models of transient and two-phase CO2 behaviour are important for saf...
AbstractThe objective of the present study is to gain an understanding on the effect of impurities d...
Pressurized liquefied gases such as carbon dioxide are transported at a pressure above their saturat...
Key to the transport phase of carbon capture and storage (CCS) is understanding the behavior of liqu...
A numerical benchmark study has been performed, comparing results from the OLGA pipeline simulator t...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
AbstractA model for two-phase carbon dioxide transport with phase transfer in pipelines is presented...
A model for two-phase carbon dioxide transport with phase transfer in pipelines is presented. The st...
AbstractWe describe the results of depressurizing an onshore 50km long, 24 inches buried pipeline fr...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractThe present paper concerns the importance of a combined modelling and experimental effort to...
AbstractPressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen ha...
Pressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen have been ...
In this work the Schlumberger flow assurance tool OLGA and SINTEF Energy Research in-house CFD tool ...
AbstractThe development, testing and validation of a two-fluid transient flow model for simulating o...
AbstractAccurate knowledge and models of transient and two-phase CO2 behaviour are important for saf...
AbstractThe objective of the present study is to gain an understanding on the effect of impurities d...
Pressurized liquefied gases such as carbon dioxide are transported at a pressure above their saturat...
Key to the transport phase of carbon capture and storage (CCS) is understanding the behavior of liqu...