dc.creatorMartinez Galeano, Yohana
dc.creatorCornaglia, Laura Maria
dc.creatorTarditi, Ana Maria
dc.date.accessioned2018-05-28T19:45:29Z
dc.date.accessioned2018-11-06T14:24:58Z
dc.date.available2018-05-28T19:45:29Z
dc.date.available2018-11-06T14:24:58Z
dc.date.created2018-05-28T19:45:29Z
dc.date.issued2016-08
dc.identifierMartinez Galeano, Yohana; Cornaglia, Laura Maria; Tarditi, Ana Maria; NaA zeolite membranes synthesized on top of APTES-modified porous stainless steel substrates; Elsevier Science; Journal of Membrane Science; 512; 8-2016; 93-103
dc.identifier0376-7388
dc.identifierhttp://hdl.handle.net/11336/46312
dc.identifierCONICET Digital
dc.identifierCONICET
dc.identifier.urihttp://repositorioslatinoamericanos.uchile.cl/handle/2250/1886123
dc.description.abstractNaA zeolite membranes were synthesized on top of both disk and tubular porous stainless steel substrates by the secondary growth method. The support seed stage was optimized, considering the seed synthesis conditions and the deposition method. The formation of the NaA zeolite on both the membrane and the residual powder collected at the bottom of the vessel after synthesis was corroborated by X-ray diffraction (XRD). Scanning electron microscopy (SEM) revealed the formation of a film with well-defined crystals with a cubic morphology characteristic of the NaA zeolite. The support modification with 3-aminopropyltriethoxysilane improved the morphology and stability of the NaA zeolite membranes synthesized on top of porous stainless steel substrates. When vacuum was applied only in the last hydrothermal synthesis stage, a smooth zeolite layer was obtained on top of porous stainless steel supports. The single gas (H2, N2, CO2 and CH4) and mixture (H2/N2 and H2/CH4) perm-selective properties of the tubular membranes were evaluated as a function of temperature and pressure. Separation factors higher than the Knudsen coefficient were obtained in all membranes. The single gas H2 and CO2 permeation flux of the membranes increased with temperature indicating a preponderance of the activated diffusion over the Knudsen diffusion. The higher H2/CO2 ideal separation factors were 7.6 and 5.6 for the more selective tubular membranes, at 453 K and 100 kPa.
dc.languageeng
dc.publisherElsevier Science
dc.relationinfo:eu-repo/semantics/altIdentifier/url/http://www.sciencedirect.com/science/article/pii/S0376738816302162
dc.relationinfo:eu-repo/semantics/altIdentifier/doi/https://dx.doi.org/10.1016/j.memsci.2016.04.005
dc.rightshttps://creativecommons.org/licenses/by-nc-sa/2.5/ar/
dc.rightsinfo:eu-repo/semantics/restrictedAccess
dc.subjectHYDROGEN RECOVERY
dc.subjectNaA ZEOLITE
dc.subjectINORGANIC MEMBRANE
dc.subjectSTAINLESS STEEL SUPPORT
dc.subject3-aminopropyltriethoxysilane
dc.titleNaA zeolite membranes synthesized on top of APTES-modified porous stainless steel substrates
dc.typeArtículos de revistas
dc.typeArtículos de revistas
dc.typeArtículos de revistas


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