Cristin-resultat-ID: 1516045
Sist endret: 20. februar 2018, 17:02
NVI-rapporteringsår: 2017
Resultat
Vitenskapelig artikkel
2017

Thermodynamic assessment of the swing adsorption reactor cluster (SARC) concept for post-combustion CO2 capture

Bidragsytere:
  • Abdelghafour Zaabout
  • Matteo C. Romano
  • Schalk Willem Petrus Cloete
  • Antonio Giuffrida
  • John Morud
  • Paolo Chiesa
  • mfl.

Tidsskrift

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

Om resultatet

Vitenskapelig artikkel
Publiseringsår: 2017
Volum: 60
Sider: 74 - 92

Importkilder

Scopus-ID: 2-s2.0-85016050547

Beskrivelse Beskrivelse

Tittel

Thermodynamic assessment of the swing adsorption reactor cluster (SARC) concept for post-combustion CO2 capture

Sammendrag

This paper presents the novel swing adsorption reactor cluster (SARC) for post combustion CO2 capture. The SARC concept consists of a cluster of bubbling/turbulent multistage fluidized bed reactors which dynamically cycle a solid sorbent between carbonation and regeneration. A synergistic combination of vacuum swing through a vacuum pump and temperature swing through a heat pump is employed to ensure high process efficiency. The base case SARC configuration imposed an energy penalty of 9.64%-points on a conventional coal-fired power plant, which is in line with advanced amine-based absorption processes. Sensitivity analyses showed that significant potential for further improvements (∼1.5%-points) exist through mechanisms such as an increase in the number of reactor stages, further reductions in regeneration pressure and optimization of the cycle length. Additional efficiency improvements can also be traded for increased reactor footprint. However, future sorbent material selection studies especially for this novel process hold the largest potential for further efficiency improvements. The SARC concept is well suited to retrofitting purposes due to limited integration with the steam cycle, and the simple standalone reactor design will simplify future scale-up efforts. The concept is therefore recommended for further study.

Bidragsytere

Abdelghafour Zaabout

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Matteo C. Romano

  • Tilknyttet:
    Forfatter
    ved Politecnico di Milano

Schalk Willem Petrus Cloete

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Antonio Giuffrida

  • Tilknyttet:
    Forfatter
    ved Politecnico di Milano

John Morud

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS
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