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Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation

Nanocomposite sodalite/ceramic membranes supported on α-Al(2)O(3) tubular support were prepared via the pore-plugging hydrothermal (PPH) synthesis protocol using one interruption and two interruption steps. In parallel, thin-film membranes were prepared via the direct hydrothermal synthesis techniqu...

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Detalles Bibliográficos
Autores principales: Eterigho-Ikelegbe, Orevaoghene, Bada, Samson O., Daramola, Michael O.
Formato: Online Artículo Texto
Lenguaje:English
Publicado: MDPI 2020
Materias:
Acceso en línea:https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7692824/
https://www.ncbi.nlm.nih.gov/pubmed/33137909
http://dx.doi.org/10.3390/membranes10110312
Descripción
Sumario:Nanocomposite sodalite/ceramic membranes supported on α-Al(2)O(3) tubular support were prepared via the pore-plugging hydrothermal (PPH) synthesis protocol using one interruption and two interruption steps. In parallel, thin-film membranes were prepared via the direct hydrothermal synthesis technique. The as-synthesized membranes were evaluated for H(2)/CO(2) separation in the context of pre-combustion CO(2) capture. Scanning electron microscopy (SEM) was used to check the surface morphology while x-ray diffraction (XRD) was used to check the crystallinity of the sodalite crystals and as-synthesized membranes. Single gas permeation of H(2), CO(2), N(2) and mixture gas H(2)/CO(2) was used to probe the quality of the membranes. Gas permeation results revealed nanocomposite membrane prepared via the PPH synthesis protocols using two interruption steps displayed the best performance. This was attributed to the enhanced pore-plugging effect of sodalite crystals in the pores of the support after the second interruption step. The nanocomposite membrane displayed H(2) permeance of 7.97 × 10(−7) mol·s(−1)·m(−2)·Pa(−1) at 100 °C and 0.48 MPa feed pressure with an ideal selectivity of 8.76. Regarding H(2)/CO(2) mixture, the H(2) permeance reduced from 8.03 × 10(−7) mol·s(−1)·m(−2)·Pa(−1) to 1.06 × 10(−7) mol·s(−1)·m(−2)·Pa(−1) at 25 °C and feed pressure of 0.18 MPa. In the presence of CO(2), selectivity of the nanocomposite membrane reduced to 4.24.