The Optimization of Dispersion and Application Techniques for Nanocarbon-Doped Mixed Matrix Gas Separation Membranes

dc.bibliographicCitation.firstPage87
dc.bibliographicCitation.issue1
dc.bibliographicCitation.journalTitleMembraneseng
dc.bibliographicCitation.volume12
dc.contributor.authorHammerstein, Ruben
dc.contributor.authorSchubert, Tim
dc.contributor.authorBraun, Gerd
dc.contributor.authorWolf, Tobias
dc.contributor.authorBarbe, Stéphan
dc.contributor.authorQuade, Antje
dc.contributor.authorFoest, Rüdiger
dc.contributor.authorKarousos, Dionysios S.
dc.contributor.authorFavvas, Evangelos P.
dc.date.accessioned2023-03-07T05:08:43Z
dc.date.available2023-03-07T05:08:43Z
dc.date.issued2022
dc.description.abstractIn this work, supported cellulose acetate (CA) mixed matrix membranes (MMMs) were prepared and studied concerning their gas separation behaviors. The dispersion of carbon nanotube fillers were studied as a factor of polymer and filler concentrations using the mixing methods of the rotor–stator system (RS) and the three-roll-mill system (TRM). Compared to the dispersion quality achieved by RS, samples prepared using the TRM seem to have slightly bigger, but fewer and more homogenously distributed, agglomerates. The green γ-butyrolactone (GBL) was chosen as a polyimide (PI) polymer-solvent, whereas diacetone alcohol (DAA) was used for preparing the CA solutions. The coating of the thin CA separation layer was applied using a spin coater. For coating on the PP carriers, a short parameter study was conducted regarding the plasma treatment to affect the wettability, the coating speed, and the volume of dispersion that was applied to the carrier. As predicted by the parameter study, the amount of dispersion that remained on the carriers decreased with an increasing rotational speed during the spin coating process. The dry separation layer thickness was varied between about 1.4 and 4.7 µm. Electrically conductive additives in a non-conductive matrix showed a steeply increasing electrical conductivity after passing the so-called percolation threshold. This was used to evaluate the agglomeration behavior in suspension and in the applied layer. Gas permeation tests were performed using a constant volume apparatus at feed pressures of 5, 10, and 15 bar. The highest calculated CO2/N2 selectivity (ideal), 21, was achieved for the CA membrane and corresponded to a CO2 permeability of 49.6 Barrer.eng
dc.description.versionpublishedVersioneng
dc.identifier.urihttps://oa.tib.eu/renate/handle/123456789/11711
dc.identifier.urihttp://dx.doi.org/10.34657/10744
dc.language.isoeng
dc.publisherBasel : MDPI
dc.relation.doihttps://doi.org/10.3390/membranes12010087
dc.relation.essn2077-0375
dc.rights.licenseCC BY 4.0 Unported
dc.rights.urihttps://creativecommons.org/licenses/by/4.0
dc.subject.ddc570
dc.subject.otherCellulose acetateeng
dc.subject.otherCNT dispersioneng
dc.subject.otherGas separationeng
dc.subject.otherMixed matrix membranes (MMMs)eng
dc.subject.otherPlasma treatmenteng
dc.subject.otherPolyimideeng
dc.subject.otherRotor-stator system (RS)eng
dc.subject.otherSpin coatingeng
dc.subject.otherSupported thin filmseng
dc.subject.otherThree-roll-mill (TRM)eng
dc.titleThe Optimization of Dispersion and Application Techniques for Nanocarbon-Doped Mixed Matrix Gas Separation Membraneseng
dc.typeArticleeng
dc.typeTexteng
tib.accessRightsopenAccess
wgl.contributorINP
wgl.subjectBiowissenschaften/Biologieger
wgl.typeZeitschriftenartikelger
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