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dc.contributor.authorLei, Linfeng
dc.contributor.authorLindbråthen, Arne
dc.contributor.authorHillestad, Magne
dc.contributor.authorHe, Xuezhong
dc.date.accessioned2022-02-17T17:49:36Z
dc.date.available2022-02-17T17:49:36Z
dc.date.created2021-03-04T15:05:44Z
dc.date.issued2021
dc.identifier.issn0376-7388
dc.identifier.urihttps://hdl.handle.net/11250/2979831
dc.description.abstractAsymmetric carbon molecular sieve (CMS) membranes prepared from cellulose hollow fiber precursors were investigated for H2/CO2 separation in this work. The prepared carbon membrane shows excellent separation performance with H2 permeance of 111 GPU and an H2/CO2 selectivity of 36.9 at 10 bar and 110 °C dry mixed gas. This membrane demonstrates high stability under a humidified gas condition at 90 °C and the pressure of up to 14 bar. A two-stage carbon membrane system was evaluated to be techno-economically feasible to produce high-purity H2 (>99.5 vol%) by HYSYS simulation, and the minimum specific H2 purification cost of 0.012 $/Nm3 H2 produced was achieved under the optimal operating condition. Sensitivity analysis on the H2 loss and H2 purity indicates that such membrane is still less cost-effective to achieve ultrapure hydrogen (e.g., >99.8 vol%) unless the higher operating temperatures for carbon membrane systems are applied.en_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.titleCarbon Molecular Sieve Membranes for Hydrogen Purification from a Steam Methane Reforming Processen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.source.journalJournal of Membrane Scienceen_US
dc.identifier.doihttp://dx.doi.org/10.1016/j.memsci.2021.119241
dc.identifier.cristin1895665
cristin.ispublishedfalse
cristin.fulltextpostprint
cristin.qualitycode2


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Navngivelse 4.0 Internasjonal
Except where otherwise noted, this item's license is described as Navngivelse 4.0 Internasjonal