Highly permeable tubular silicalite-1 membranes for CO 2 capture

• Published in: The Science of the total environment 2019-08, Vol.676, p.305
• Main Authors: Tawalbeh, Muhammad, Tezel, F Handan, Al-Ismaily, M, Kruczek, Boguslaw
• Format: Article
• Language: English
• ISSN: 1879-1026
• DOI: 10.1016/j.scitotenv.2019.04.290

Membranes represent one of the most promising alternatives for CO separation and capture. Zeolites membranes, in particular, that can withstand high temperatures and pressures, offer energy efficient way to capture CO compared to conventional separation techniques such as amine absorption. In this work, silicalite-1/ceramic composite membranes were prepared on the inner surface of zirconium oxide and/or titanium oxide tubular supports by a pore plugging hydrothermal synthesis. Five types of supports with different pore sizes ranging from 0.14 to 1.4 μm, were studied. The synthesized membranes were characterized by scanning electron microscope (SEM), electron diffraction spectrometer (EDS), x-ray diffraction (XRD), and gas permeation with pure and mixed gas feeds. All membranes showed high concentrations of Si within the active layer of the support, suggesting successful pore-plugging of the membranes. The greater the pore size of the active layer of the support, the greater was the concentration of Si observed. In addition, large coffin-shape crystals, which are characteristics of silicalite-1, were also observed on top of each membrane. The analysis of XRD micrographs revealed that the crystals were mostly oriented with either the a- or b-axes perpendicular to the membrane surface, which is desirable from the point of view of minimizing the resistance to gas transport through the zeolite membrane. Except for the membranes synthesized using the supports with 0.14 μm pores, all membranes were very selective with CO /N permselectivities up to 30 at low-pressure differentials. At the same time, the membranes were very permeable with CO permeance in the order of 10  mol m  Pa  s . Assuming the thickness of the selective layer to be equivalent to the thickness of the active layer of the support, all membranes fell above the revised Robeson upper-bound line for CO /N separation.