Add to ORKGA 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. Copyright © 2012 Published by Elsevier Ltd
AbstractPressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen ha...
The design of safe and cost-efficient CO2-transportation systems is an integral part of CO2 capture ...
We present and discuss two-phase flow models to simulate transient flow of CO2-rich mixtures in pipe...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
A numerical benchmark study has been performed, comparing results from the OLGA pipeline simulator t...
A model for two-phase carbon dioxide transport with phase transfer in pipelines is presented. The st...
AbstractA model for two-phase carbon dioxide transport with phase transfer in pipelines is presented...
AbstractWe describe the results of depressurizing an onshore 50km long, 24 inches buried pipeline fr...
In this work the Schlumberger flow assurance tool OLGA and SINTEF Energy Research in-house CFD tool ...
This dataset contains data from depressurization of pure CO2 and nitrogen in a tube from a gaseous a...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractThe objective of the present study is to gain an understanding on the effect of impurities d...
Key to the transport phase of carbon capture and storage (CCS) is understanding the behavior of liqu...
This dataset contains data from depressurization of two CO2 mixtures in a tube from a gaseous and a ...
Pressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen have been ...
AbstractPressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen ha...
The design of safe and cost-efficient CO2-transportation systems is an integral part of CO2 capture ...
We present and discuss two-phase flow models to simulate transient flow of CO2-rich mixtures in pipe...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
A numerical benchmark study has been performed, comparing results from the OLGA pipeline simulator t...
A model for two-phase carbon dioxide transport with phase transfer in pipelines is presented. The st...
AbstractA model for two-phase carbon dioxide transport with phase transfer in pipelines is presented...
AbstractWe describe the results of depressurizing an onshore 50km long, 24 inches buried pipeline fr...
In this work the Schlumberger flow assurance tool OLGA and SINTEF Energy Research in-house CFD tool ...
This dataset contains data from depressurization of pure CO2 and nitrogen in a tube from a gaseous a...
AbstractThe proper modeling of CO2 depressurization is very important for the design for safety of a...
AbstractThe objective of the present study is to gain an understanding on the effect of impurities d...
Key to the transport phase of carbon capture and storage (CCS) is understanding the behavior of liqu...
This dataset contains data from depressurization of two CO2 mixtures in a tube from a gaseous and a ...
Pressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen have been ...
AbstractPressure-release experiments of CO2 with impurity contents of 10, 20 and 30 mol% nitrogen ha...
The design of safe and cost-efficient CO2-transportation systems is an integral part of CO2 capture ...
We present and discuss two-phase flow models to simulate transient flow of CO2-rich mixtures in pipe...