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dc.contributor.authorKajama, Mohammed
dc.contributor.authorNwogu, Ngozi Claribelle
dc.contributor.authorGobina, Edward
dc.date.accessioned2016-04-20T10:52:30Z
dc.date.available2016-04-20T10:52:30Z
dc.date.issued2014-07-11
dc.identifier.citationKAJAMA, M.N., NWOGU, N.C. and GOBINA, E., 2014. Gas permeation study using porous ceramic membranes. Energy and Environment Research, Vol 4 (3), pp. 43-49.en
dc.identifier.issn1927-0569en
dc.identifier.issn1927-0577en
dc.identifier.urihttp://hdl.handle.net/10059/1448
dc.description.abstractA 6000 nm ceramic membrane was repaired with boehmite solution (ALOOH) through the repeat dip-coating technique. The permeance of hydrogen (H2) and carbon dioxide (CO2) were obtained through the membrane in relation to average pressure at room temperature for the support membrane and as cracked membrane. A repair process was carried out on the cracked membrane by same dip coating process and results obtained after first and second dips. The permeance of the support membrane obtained ranged between 1.50 to 3.04 × 10-7 mol m-2 s-1 Pa-1. However, as a result of a crack that occurred during the removal of the membrane from the reactor, the permeance increased from 2.96 to 5.82 10-7 mol m-2 s-1 Pa-1. Further application of boehmite solution on the membrane lead to an improvement on the surface of the membrane with some degree and surface cracks were reduced. This also decreased the permeance to 1.26 – 3.39 × 10-8 mol m-2 s-1 Pa-1 after the second dip. Consequently, another silica based modified membrane was used for carbon dioxide and nitrogen (N2) permeation. The plots show that carbon dioxide permeated faster than the other gases, indicating dominance of a more selective adsorptive transport mechanism. Accordingly, results obtained show an appreciable high carbon dioxide permeance of 3.42 × 10-6 mol m-2 s-1 Pa-1 at a relatively low pressure when compared to nitrogenconfirming that the membrane has so far exhibited a high permeability, selectivity and high CO2 gas recovery. The permselectivities of CO2 over H2 at room temperature was also obtained which were higher than the Knudsen selectivity.en
dc.description.sponsorshipPetroleum Technology Development Fund (PTDF) Nigeriaen
dc.language.isoenen
dc.publisherCanadian Centre of Science and Educationen
dc.rightshttps://creativecommons.org/licenses/by/4.0/en
dc.rightsAttribution 4.0 International*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/*
dc.subjectCeramic membranesen
dc.subjectGas permeationen
dc.subjectHydrogen selectivityen
dc.subjectCarbon dioxide selectivityen
dc.subjectDefect repairen
dc.titleGas permeation study using ceramic membranes.en
dc.typeJournal articlesen
dc.publisher.urihttp://dx.doi.org/10.5539/eer.v4n3p43en
refterms.accessExceptionNAen
refterms.depositExceptionNAen
refterms.panelUnspecifieden
refterms.technicalExceptionNAen
refterms.versionNAen
rioxxterms.typeJournal Article/Reviewen


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