Cargando…

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...

Descripción completa

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
_version_ 1783614602166140928
author Eterigho-Ikelegbe, Orevaoghene
Bada, Samson O.
Daramola, Michael O.
author_facet Eterigho-Ikelegbe, Orevaoghene
Bada, Samson O.
Daramola, Michael O.
author_sort Eterigho-Ikelegbe, Orevaoghene
collection PubMed
description 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.
format Online
Article
Text
id pubmed-7692824
institution National Center for Biotechnology Information
language English
publishDate 2020
publisher MDPI
record_format MEDLINE/PubMed
spelling pubmed-76928242020-11-28 Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation Eterigho-Ikelegbe, Orevaoghene Bada, Samson O. Daramola, Michael O. Membranes (Basel) Article 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. MDPI 2020-10-29 /pmc/articles/PMC7692824/ /pubmed/33137909 http://dx.doi.org/10.3390/membranes10110312 Text en © 2020 by the authors. Licensee MDPI, Basel, Switzerland. This article is an open access article distributed under the terms and conditions of the Creative Commons Attribution (CC BY) license (http://creativecommons.org/licenses/by/4.0/).
spellingShingle Article
Eterigho-Ikelegbe, Orevaoghene
Bada, Samson O.
Daramola, Michael O.
Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title_full Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title_fullStr Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title_full_unstemmed Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title_short Preparation and Evaluation of Nanocomposite Sodalite/α-Al(2)O(3) Tubular Membranes for H(2)/CO(2) Separation
title_sort preparation and evaluation of nanocomposite sodalite/α-al(2)o(3) tubular membranes for h(2)/co(2) separation
topic Article
url https://www.ncbi.nlm.nih.gov/pmc/articles/PMC7692824/
https://www.ncbi.nlm.nih.gov/pubmed/33137909
http://dx.doi.org/10.3390/membranes10110312
work_keys_str_mv AT eterighoikelegbeorevaoghene preparationandevaluationofnanocompositesodaliteaal2o3tubularmembranesforh2co2separation
AT badasamsono preparationandevaluationofnanocompositesodaliteaal2o3tubularmembranesforh2co2separation
AT daramolamichaelo preparationandevaluationofnanocompositesodaliteaal2o3tubularmembranesforh2co2separation