(520c) The CO2 and H2 Permeability of Membranes Composed of Polyfluoroacrylate, Perfluoropolyether (PFPE), PFPE-Plasticized Amorphous Teflon, and Polyfluoroalkoxyphosphazene | AIChE

(520c) The CO2 and H2 Permeability of Membranes Composed of Polyfluoroacrylate, Perfluoropolyether (PFPE), PFPE-Plasticized Amorphous Teflon, and Polyfluoroalkoxyphosphazene

Authors 

Lugert, E. - Presenter, University of Minnesota
Buhlmann, P. - Presenter, University of Minnesota


Membranes could be an integral part of the coal gasification/water-gas-shift reaction process to transform coal, oxygen and water feed streams into hydrogen for fuel and CO2 for sequestration. The objective of this work is to design polymeric membranes that have very high CO2 permeability and high selectivity toward CO2 (i.e. very low H2 permeability). It is our hypothesis that the favorable thermodynamic interactions that enable certain polymers to dissolve in dense CO2 at extremely high pressure will also allow membranes composed of these polymers to exhibit high CO2 permeability at low pressure. Candidates include perfluoro polyether (PFPE), polyfluoroalkoxy phosphazene (PFAP), poly(fluoroacrylate) (PFA) and PFPE-plasticized Teflon AF2400. PFPE is a liquid oligomer that was transformed into a diacrylate and then cross-linked to form flexible membranes. PFAP and PFA were processed into films via dip coating or spin coating. Although PFA is known to be one of the most CO2-philic amorphous polymers ever identified, and the solubility of PFPE is comparable to PDMS at lower molecular weights, the CO2-permeability of these membranes has not (to the best of our knowledge) been previously established.

The CO2 and H2 permeability values of these fluorinated membranes were determined using a constant volume apparatus or constant pressure apparatus. These constant volume experiments were conducted with a single gas at 295K and CO2 (or H2) with partial pressure gradients no greater than 450 kPa. Ideal selectivity values were determined as the ratio of CO2 permeability to H2 permeability. The mixed gas constant pressure experiments were conducted within a temperature range of 310 to 423 K and CO2 (or H2) partial pressure gradients near atmospheric conditions. Permselectivity values were determined as the ratio of CO2 permeability to H2 permeability.

PFPE membranes exhibited relatively high permeability values (comparable to PDMS), but CO2/H2 selectivity values did not exceed 5. Despite its incredible CO2-philicity, the PFA membrane exhibited disappointingly low permeance and selectivity values. Results for the PFPE-plasticized amorphous Teflon and the PFAP membranes will also be presented.