Cristin-resultat-ID: 1807327
Sist endret: 14. juni 2020, 12:14
NVI-rapporteringsår: 2020
Resultat
Vitenskapelig artikkel
2020

Production of MOF Adsorbent Spheres and Comparison of Their Performance with Zeolite 13X in a Moving-Bed TSA Process for Postcombustion CO2 Capture

Bidragsytere:
  • Giorgia Mondino
  • Aud I. Spjelkavik
  • Terje Didriksen
  • Shreenath Krishnamurthy
  • Ruth Elisabeth Stensrød
  • Carlos Adolfo Grande
  • mfl.

Tidsskrift

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

Om resultatet

Vitenskapelig artikkel
Publiseringsår: 2020
Publisert online: 2020
Trykket: 2020
Volum: 59
Hefte: 15
Sider: 7198 - 7211
Open Access

Importkilder

Scopus-ID: 2-s2.0-85084672177

Beskrivelse Beskrivelse

Tittel

Production of MOF Adsorbent Spheres and Comparison of Their Performance with Zeolite 13X in a Moving-Bed TSA Process for Postcombustion CO2 Capture

Sammendrag

Well-shaped 300–700 μm spheres of aggregated metal–organic framework CPO-27-Ni crystallites have been produced using a spray-granulation method with cross-bonded alginate as the binder. The spheres are suitable for use in a moving-bed temperature-swing adsorption (MBTSA) process for postcombustion CO2 capture. The adsorption isotherm data of CO2, N2 ,and H2O have been measured in the temperature intervalof 30–120 °C, and adsorption kinetics have been estimated from breakthrough measurements. The adsorption data together with the physical characteristics of the spheres (pore-size distribution and porosity) have been used to simulate the performance of a MBTSA process utilizing the CPO-27-Ni/alginate spheres as adsorbent and compared to similar simulations using Zeolite 13X spheres. Simulations have been carried out in a natural gas-fired power plant (NGCC) context. The process simulations indicate that the net electric efficiency of the NGCC plant with a MBTSA process utilizing the CPO-27-Ni/alginate spheres is similar to that of a MBTSA process utilizing Zeolite 13X adsorbent, 56.1% and 55.9%, respectively, which are slightly higher than the net efficiency of the benchmark case NGCC with a MEA-based solvent process of 54.7%

Bidragsytere

Giorgia Mondino

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

Aud I. Spjelkavik

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Terje Didriksen

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS
Aktiv cristin-person

Shreenath Krishnamurthy

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS

Ruth Elisabeth Stensrød

  • Tilknyttet:
    Forfatter
    ved Prosessteknologi ved SINTEF AS
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