296023 Covanlently Linked Acrylate Derivitized Psf and Amine Functionalized Mesorporous MCM-41 Based Mixed Matrix Membranes For CO2 Separation
296023 Covanlently Linked Acrylate Derivitized Psf and Amine Functionalized Mesorporous MCM-41 Based Mixed Matrix Membranes For CO2 Separation
Monday, June 10, 2013
Ballroom (Grove Hotel)
Mixed matrix membranes (MMMs), comprising molecular sieving materials embedded in a polymer matrix, are promising candidates with substantial potential to overcome the Robeson’s upper-bound trade-off. These membranes combine the easy processability of the polymers with high flux/selectivity of the inorganic porous materials. However, due to the difference in physio-chemical properties, the formation of defect-free MMMs has proven to be challenging. The poor interfacial contact between the polymer and the filler results in the formation of so-called microvoids which significantly lower the membrane separation performance. In this work, MMMs composed of acrylate derivatized polysulfone and mesoporous MCM-41 were prepared by solution casting. The voids at the polymer-filler interface were removed by the introduction of covalent linkages between the modified polymer and the functionalized fillers. MCM-41 was chosen as a filler because of several inherent advantages, such as high specific surface area, high CO2 adsorption, high mechanical and thermal stability and easy surface modificatio. Gas permeation results and SEM images of the synthesized MMMs confirmed a good adhesion and dispersion of the fillers within the polymer matrix. SEM results showed that the interfacial voids were mostly eliminated with a visible, non-porous, defect-free structure, which is ideally suited for gas separation membranes. In comparison to MMMs with unmodified MCM-41, covalently linked MCM-41 fillers rendered the MMMs significantly higher CO2/CH4 and CO2/N2 selectivities due to the presence of a covalent link between the -NH2 group of the filler and the acrylate of the polymer. The highest ideal selectivities obtained here for CO2/N2 and CO2/CH4 were 32.97 and 31.48 (CO2 permeability = 9.13 Barrer), respectively. The performance of membranes under mixed gas feeds and different operating temperatures was also studied.
See more of this Session: Poster Session: Membrane Synthesis
See more of this Group/Topical: Poster Submissions
See more of this Group/Topical: Poster Submissions
