This dataset contains data from depressurization of two CO2 mixtures in a tube from a gaseous and a dense-liquid state. The data are described in the accompanying paper (DOI: 10.1016/j.ijggc.2021.103361). The initial state is 12 MPa and 25 degrees C. Mixture 1: CO2 with 1.8 mol % N2 (Experiment 9). Mixture 2: CO2 with 1.92 % He (Experiment 12)
Span and Wagner equation of state (SW EOS) have been used to investigate changes in the thermodynami...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
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...
The design of safe and cost-efficient CO2-transportation systems is an integral part of CO2 capture ...
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...
We present and discuss two-phase flow models to simulate transient flow of CO2-rich mixtures in pipe...
AbstractAccurate knowledge and models of transient and two-phase CO2 behaviour are important for saf...
AbstractThe development, testing and validation of a two-fluid transient flow model for simulating o...
AbstractSpan and Wagner equation of state (SW EOS) have been used to investigate changes in the ther...
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...
Decompression of CO2 pipelines is studied both experimentally and numerically to provide a partially...
Carbon Capture and Storage (CCS) is widely seen as an effective technique to reduce what is perceive...
Span and Wagner equation of state (SW EOS) have been used to investigate changes in the thermodynami...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
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...
The design of safe and cost-efficient CO2-transportation systems is an integral part of CO2 capture ...
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...
We present and discuss two-phase flow models to simulate transient flow of CO2-rich mixtures in pipe...
AbstractAccurate knowledge and models of transient and two-phase CO2 behaviour are important for saf...
AbstractThe development, testing and validation of a two-fluid transient flow model for simulating o...
AbstractSpan and Wagner equation of state (SW EOS) have been used to investigate changes in the ther...
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...
Decompression of CO2 pipelines is studied both experimentally and numerically to provide a partially...
Carbon Capture and Storage (CCS) is widely seen as an effective technique to reduce what is perceive...
Span and Wagner equation of state (SW EOS) have been used to investigate changes in the thermodynami...
AbstractA numerical benchmark study has been performed, comparing results from the OLGA pipeline sim...
In this work the Schlumberger flow assurance tool OLGA and SINTEF Energy Research in-house CFD tool ...