4.7 Article

Novel MMM using CO2 selective SSZ-16 and high-performance 6FDA-polyimide for CO2/CH4 separation

Journal

SEPARATION AND PURIFICATION TECHNOLOGY
Volume 254, Issue -, Pages -

Publisher

ELSEVIER
DOI: 10.1016/j.seppur.2020.117582

Keywords

6FDA-polyimide; Mixed matrix membrane; Zeolite; SSZ-16; CO2/CH4 separation

Funding

  1. Education, Audiovisual and Culture Executive Agency within the Erasmus Mundus Doctorate in Membrane Engineering-EUDIME (ERASMUS MUNDUS Programme 2009-2013) [2011-0014, 2012-1719]
  2. Operational Programme Prague-Competitiveness [CZ.2.16/3.1.00/24501]
  3. National Program of Sustainability [NPU I LO1613, MSMT-43760/2015]
  4. Ministry of Education, Youth and Sports of the Czech Republic
  5. EU - European Structural and Investment Funds - Operational Programme Research, Development and Education - project SPETEP [CZ.02.1.01/0.0/0.0/16_026/0008413]

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The study investigates a new mixed matrix membrane with SSZ-16 zeolite addition to improve gas separation performance. While higher filler loadings slightly lower permeability, excessively high loadings can lead to a drop in selectivity due to defective polymer-filler interfaces.
The development, characterization, and CO2/CH4 separation properties of a new mixed matrix membrane (MMM), comprises of 6FDA-DAM:DABA and small pore zeolite SSZ-16 were investigated. The MMMs were prepared with different zeolite loadings to study the filler content effects on the membrane physical and gas transport properties. Consequently, their gas separation performances were investigated at several transmembrane pressures (2, 4, 6 and 8 bar) using different binary feed gas compositions (25/75, 50/50, 75/25 vol.% of CO2/CH4) at 25 degrees C. Besides improving the membrane physical properties, SSZ-16 addition is proven to enhance the gas separation performance effectively. The MMM with 5 wt.% SSZ-16 presents an excellent filler dispersion and increased CO2 permeability by almost 2-fold while maintaining its high CO2/CH4 selectivity, with respect to the unfilled membrane (P-CO2 = 199.4 Barrer; alpha(CO2/CH4) = 35.9). Higher filler loadings show slightly lower permeability, indicating a possible polymer rigidification in the filler-polymer region. Most importantly, MMM with the highest loading presents selectivity drop by similar to 50% due to defective polymer-filler interfaces, which directly increased the CH4 permeability, concluding SSZ-16 addition is able to achieve the ideal MMM improvement only at low loadings. All the findings concerning different feed composition and transmembrane pressures are presented and discussed accordingly.

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