Published October 2012 | Version v1
Journal article

Technico-economical assessment of MFI-type zeolite membranes for CO2 capture from post-combustion flue gases

  • 1. Univ Lyon 1, Inst Rech Catalyse et Environm Lyon IRCELYON, CNRS, UMR 5256, F-69626 Villeurbanne, (France)
  • 2. CEA Marcoule, DTCD, SPDE, Lab Fluides Supercrit et Me, F-30207 Bagnols Sur Ceze, (France)
  • 3. PALL EXEKIA, F-65460 Bazet, (France)
  • 4. LAB SA, F-69006 Lyon, (France)
  • 5. TREDI, Serv Rech, F-54505 Vandoeuvre Les Nancy, (France)

Description

A detailed survey of the effect of moisture on the CO2/N2 permeation and separation performance of Mobile Five (MFI) zeolite membranes in view of downstream post-combustion CO2 capture applications in power plants and incinerators is presented. The membranes, displaying a nano-composite architecture, have been prepared on α-alumina tubes by pore-plugging hydrothermal synthesis at 443 K for 89 h using a precursor clear solution with molar composition 1 SiO2:0.45 tetrapropylammonium hydroxide:27.8 H2O. The synthesized membranes present reasonable permeation and CO2/N2 separation properties even in the presence of high water concentrations in the gas stream. A critical discussion is also provided on the technico-economical feasibility (i.e., CO2 recovery, CO2 purity in the permeate, module volume, and energy consumption) of a membrane cascade unit for CO2 capture and liquefaction/supercritical storage from standard flue gases emitted from an incinerator. Our results suggest that the permeate pressure should be kept under primary vacuum to promote the CO2 driving force within the membrane. (authors)

Availability note (English)

Available from doi: http://dx.doi.org/10.1002/aic.12805

Additional details

Identifiers

Publishing Information

Journal Title
AIChE Journal
Journal Volume
58
Journal Issue
no.10
Journal Page Range
p. 3183-3194
ISSN
0001-1541

Optional Information

Notes
54 refs.