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dc.contributor.authorXu, Wenqi
dc.contributor.authorLindbråthen, Arne
dc.contributor.authorJanakiram, Saravanan
dc.contributor.authorAnsaloni, Luca
dc.contributor.authorLei, Linfeng
dc.contributor.authorDeng, Liyuan
dc.date.accessioned2023-12-19T09:43:37Z
dc.date.available2023-12-19T09:43:37Z
dc.date.created2023-10-04T13:45:41Z
dc.date.issued2023
dc.identifier.issn0009-2509
dc.identifier.urihttps://hdl.handle.net/11250/3108150
dc.description.abstractIn this work, a membrane separation process is designed and optimized to purify dark fermentative biohydrogen by removing CO2. A CO2-selective PVAm-based nanocomposite membrane was selected considering its high CO2/H2 separation performance and unique features suitable for the process. We tested the membrane performances under the separation conditions to provide a more accurate simulation basis. Several design scenarios were investigated. A two-stage process with a recycle stream is determined as the optimal design, in which the specific cost for purifying H2 to 99.5 vol% with H2 loss of <10% reaches only 0.156 $/Nm3. The techno-economic feasibility study of biohydrogen purification with simultaneous CO2 capture was also performed through an alternative design by introducing a 3rd-stage using the same membrane or an H2-selective membrane. Adding a 3rd-stage membrane can capture and purify CO2 as a side product of various purities, which further decreases the H2 loss, leading to additional economic benefits.en_US
dc.language.isoengen_US
dc.publisherElsevier B. V.en_US
dc.rightsNavngivelse 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by/4.0/deed.no*
dc.titleMembrane process design for biohydrogen purification with simultaneous CO2 capture: Feasibility and techno-economic assessmenten_US
dc.title.alternativeMembrane process design for biohydrogen purification with simultaneous CO2 capture: Feasibility and techno-economic assessmenten_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.source.volume282en_US
dc.source.journalChemical Engineering Science (CES)en_US
dc.identifier.doi10.1016/j.ces.2023.119219
dc.identifier.cristin2181669
dc.relation.projectNorges forskningsråd: 294533en_US
dc.source.articlenumber119219en_US
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode2


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