Cristin-resultat-ID: 1097004
Sist endret: 18. februar 2015, 00:35
NVI-rapporteringsår: 2013
Resultat
Vitenskapelig artikkel
2013

Experimental Demonstration of a Novel Gas Switching Combustion Reactor for Power Production with Integrated CO2 Capture

Bidragsytere:
  • Abdelghafour Zaabout
  • Schalk Willem Petrus Cloete
  • Stein Tore Johansen
  • MV Annaland
  • F Gallucci og
  • Shahriar Amini

Tidsskrift

Industrial & Engineering Chemistry Research
ISSN 0888-5885
e-ISSN 1520-5045
NVI-nivå 2

Om resultatet

Vitenskapelig artikkel
Publiseringsår: 2013
Volum: 52
Hefte: 39
Sider: 14241 - 14250
Open Access

Importkilder

Scopus-ID: 2-s2.0-84885197148
Isi-ID: 000326300400041

Beskrivelse Beskrivelse

Tittel

Experimental Demonstration of a Novel Gas Switching Combustion Reactor for Power Production with Integrated CO2 Capture

Sammendrag

This paper experimentally demonstrates the feasibility of a novel gas switching combustion (GSC) reactor as an alternative to the traditional chemical looping combustion (CLC) process for power production with integrated CO2 capture. Whereas the CLC process circulates an oxygen carrier material between two fluidized bed reactors, where it is exposed to separate fuel and air streams, the GSC concept employs a single dense fluidized bed reactor where the oxygen carrier is periodically exposed to fuel and air streams. A lab-scale GSC reactor was operated autothermally (without any external temperature supply) to continuously convert cold feed gases into hot product gases, which would be suitable for driving a downstream power cycle. A parametric study was carried out to further investigate the behavior of the GSC concept. The reactor achieved a high CO2 capture efficiency (97.2%) and purity (98.2%) even without the use of a purging stage between the oxidation and reduction stages. A small amount of carbon deposition (around 1%) had a slight negative effect on the CO2 capture efficiency. Finally, the operation of a cluster of GSC reactors capable of delivering two steady process streams to downstream process equipment is discussed.

Bidragsytere

Abdelghafour Zaabout

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS
  • Tilknyttet:
    Forfatter
    ved Technische Universiteit Eindhoven

Schalk Willem Petrus Cloete

  • Tilknyttet:
    Forfatter
    ved Institutt for energi- og prosessteknikk ved Norges teknisk-naturvitenskapelige universitet

Stein Tore Johansen

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

MV Annaland

  • Tilknyttet:
    Forfatter
    ved Technische Universiteit Eindhoven

F Gallucci

  • Tilknyttet:
    Forfatter
    ved Technische Universiteit Eindhoven
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