Cristin-resultat-ID: 1963746
Sist endret: 24. februar 2022, 09:33
NVI-rapporteringsår: 2021
Resultat
Vitenskapelig artikkel
2021

Design of a multi-user CO2 intermediate storage facility in the Grenland region of Norway

Bidragsytere:
  • Denis Martins Fraga
  • Ragnhild Skagestad
  • Nils Henrik Eldrup
  • Anna Korre
  • Hans Aksel Haugen
  • Zhenggang Nie
  • mfl.

Tidsskrift

International Journal of Greenhouse Gas Control
ISSN 1750-5836
e-ISSN 1878-0148
NVI-nivå 1

Om resultatet

Vitenskapelig artikkel
Publiseringsår: 2021
Volum: 112
Artikkelnummer: 103514

Importkilder

Scopus-ID: 2-s2.0-85119410732

Beskrivelse Beskrivelse

Tittel

Design of a multi-user CO2 intermediate storage facility in the Grenland region of Norway

Sammendrag

This paper describes a design and pre-feasibility study of a multi-user intermediate CO2 storage facility in the Grenland region of Norway, considering upstream and downstream issues. The study focuses on the principles for designing and installing a generic hub facility so that the results can be considered at other sites. The pre-feasibility study found that design pressures of 7 and 15 bar are feasible transport conditions; moreover, it showed that economies of scale might reduce the total cost for a CO2 network. It is recognised that cooperation across the chain is crucial in managing impurities due to the likely diverse sources of CO2. An intermediate storage facility can support the continuous supply of CO2 via a pipeline system for reservoir injection, improving the integrity of the injection well and equipment and the reservoir performance. A mixed-integer linear programming optimisation model has been developed for sizing and costing intermediate storage hubs of CO2 in Grenland and shipping connections between them and stationary emitters. The model considers an aggregated flow of 2 million tonnes per annum of CO2 for 30 years. The 7 bar design pressure has shown lower total costs when compared with the 15 bar scenario. This is due to the higher costs for shipping and intermediate storage when operating at higher pressure, which is larger than the cost reduction from liquefying CO2 to a higher pressure and higher temperature than those required for a 7 bar scenario. The estimated levelised costs were 21,6 € tonne−1 at 7 bar pressure and 27,8 € tonne−1 at 15 bar pressure.

Bidragsytere

Denis Martins Fraga

  • Tilknyttet:
    Forfatter
    ved Imperial College London

Ragnhild Skagestad

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Nils Henrik Eldrup

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Anna Korre

  • Tilknyttet:
    Forfatter
    ved Imperial College London

Hans Aksel Haugen

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS
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