Why is it so extremely difficult to prepare shape-selective Al-rich zeolite membranes like LTA and FAU for gas separation?

verfasst von: J. Caro, D. Albrecht, M. Noack
Abstract: Two possible reasons for the difficulty to prepare shape-selective Al-rich zeolite membranes for gas separation are discussed. One reason is the strongly negative electric surface charge of Al-rich zeolites like LTA or FAU in aqueous media as found by zeta potential (ZP) measurements of suspended zeolite powder. This negative surface charge is expected to prevent the negatively charged silica species to enter the slits between the growing crystallites in a zeolite membrane layer. This effect can be avoided by adsorption of positively charged species called intergrowth supporting substance (ISS) neutralizing the electric surface charges of the growing zeolite membrane surface. Another problem for Al-rich membranes are extreme mismatches in the expansion coefficients between the zeolite layer and the ceramic or metal support upon drying the as synthesized membranes. The as synthesized FAU or LTA membrane layers contain water. We have simulated a membrane activation in the permeation cell by drying zeolite powder and recording in situ the XRD spectra. We found huge expansion and shrinking effects during the in situ de-watering of LTA and FAU powder samples. This observation is correlated with the experimental finding continuous damage of model membranes upon repeated re-activation cycles in vacuum at 150 °C. The model membranes consisted of a few large LTA and FAU crystals embedded into epoxy resin. After each de-watering step, (i) the fluxes of CO₂, CH₄ and N₂ increased and (ii) the ideal selectivities decreased which indicates a continuous membrane damage. However, these semi-damaged LTA and FAU membranes can still separate water from alcohols but do not show any gas separation.
Organisationseinheit(en): Institut für Physikalische Chemie und Elektrochemie
Externe Organisation(en): Leibniz-Institut für Katalyse e.V. (LIKAT Rostock)
Universität Rostock
Typ: Artikel
Journal: Separation and Purification Technology
Band: 66
Seiten: 143-147
Anzahl der Seiten: 5
ISSN: 1383-5866
Publikationsdatum: 07.04.2009
Publikationsstatus: Veröffentlicht
Peer-reviewed: Ja
ASJC Scopus Sachgebiete: Analytische Chemie, Filtration und Separation
Elektronische Version(en): https://doi.org/10.1016/j.seppur.2008.11.009 (Zugang: Geschlossen)

BibTeX

@article{c81bb091811d4e1b80e4d468482c1635,
title = "Why is it so extremely difficult to prepare shape-selective Al-rich zeolite membranes like LTA and FAU for gas separation?",
abstract = "Two possible reasons for the difficulty to prepare shape-selective Al-rich zeolite membranes for gas separation are discussed. One reason is the strongly negative electric surface charge of Al-rich zeolites like LTA or FAU in aqueous media as found by zeta potential (ZP) measurements of suspended zeolite powder. This negative surface charge is expected to prevent the negatively charged silica species to enter the slits between the growing crystallites in a zeolite membrane layer. This effect can be avoided by adsorption of positively charged species called intergrowth supporting substance (ISS) neutralizing the electric surface charges of the growing zeolite membrane surface. Another problem for Al-rich membranes are extreme mismatches in the expansion coefficients between the zeolite layer and the ceramic or metal support upon drying the as synthesized membranes. The as synthesized FAU or LTA membrane layers contain water. We have simulated a membrane activation in the permeation cell by drying zeolite powder and recording in situ the XRD spectra. We found huge expansion and shrinking effects during the in situ de-watering of LTA and FAU powder samples. This observation is correlated with the experimental finding continuous damage of model membranes upon repeated re-activation cycles in vacuum at 150 °C. The model membranes consisted of a few large LTA and FAU crystals embedded into epoxy resin. After each de-watering step, (i) the fluxes of CO2, CH4 and N2 increased and (ii) the ideal selectivities decreased which indicates a continuous membrane damage. However, these semi-damaged LTA and FAU membranes can still separate water from alcohols but do not show any gas separation.",
keywords = "FAU zeolite membranes, Ideal permselectivity, Intergrowth supporting substances, LTA, Mismatch expansion behavior, Mixture separation factor, Permporometry, Zeta potential",
author = "J. Caro and D. Albrecht and M. Noack",
year = "2009",
month = apr,
day = "7",
doi = "10.1016/j.seppur.2008.11.009",
language = "English",
volume = "66",
pages = "143--147",
journal = "Separation and Purification Technology",
issn = "1383-5866",
publisher = "Elsevier",
number = "1",
}