Cristin-resultat-ID: 1190272
Sist endret: 6. januar 2015, 03:49
NVI-rapporteringsår: 2014
Resultat
Vitenskapelig artikkel
2014

Energy and Cost Evaluation of A Low-temperature CO2 Capture Unit for IGCC plants

Bidragsytere:
  • David Olsson Berstad
  • Simon Roussanaly
  • Geir Skaugen
  • Rahul Anantharaman
  • Petter Nekså og
  • Kristin Jordal

Tidsskrift

Energy Procedia
ISSN 1876-6102
e-ISSN 1876-6102
NVI-nivå 0

Om resultatet

Vitenskapelig artikkel
Publiseringsår: 2014
Volum: 63
Sider: 2031 - 2036
Open Access

Importkilder

Scopus-ID: 2-s2.0-84922883069

Beskrivelse Beskrivelse

Tittel

Energy and Cost Evaluation of A Low-temperature CO2 Capture Unit for IGCC plants

Sammendrag

The application of CO2 capture by liquefaction has been investigated for an integrated gasification combined cycle (IGCC). Two configurations of the process are developed–one supplying CO2 at conditions suitable for pipeline transport and the second one producing liquid CO2 suitable for ship transport. The liquefaction process for CO2 capture is more efficient and compact compared to Selexol process for providing CO2 suitable for ship transport as the separation and liquefaction units are integrated in the process presented in this work. An economic analysis performed shows that CO2 capture by liquefaction is more cost efficient than corresponding Selexol-based separation processes by 9–11% in terms of the levelized cost of electricity and 35–37% in terms of CO2 avoidance costs

Bidragsytere

David Olsson Berstad

  • Tilknyttet:
    Forfatter
    ved Gassteknologi ved SINTEF Energi AS

Simon Roussanaly

  • Tilknyttet:
    Forfatter
    ved Gassteknologi ved SINTEF Energi AS

Geir Skaugen

  • Tilknyttet:
    Forfatter
    ved Gassteknologi ved SINTEF Energi AS

Rahul Anantharaman

  • Tilknyttet:
    Forfatter
    ved Gassteknologi ved SINTEF Energi AS

Petter Nekså

  • Tilknyttet:
    Forfatter
    ved Gassteknologi ved SINTEF Energi AS
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