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dc.contributor.authorHe, Xuezhong
dc.contributor.authorLei, Linfeng
dc.date.accessioned2021-02-02T13:44:45Z
dc.date.available2021-02-02T13:44:45Z
dc.date.created2020-12-08T21:15:51Z
dc.date.issued2020
dc.identifier.issn1383-5866
dc.identifier.urihttps://hdl.handle.net/11250/2725854
dc.description.abstractUtilization of the low concentration methane from coal-mining ventilation air is challenging but can significantly contribute to the mitigation of methane emissions to the atmosphere. This work focuses on the techno-economic feasibility analysis of N2-selective membrane systems for the enrichment of ventilation air methane (VAM). The feed methane concentration and gas permeance are found to significantly influence the specific methane enrichment cost, while feed pressure has the lest effect. For a stand-alone membrane system, the optimal methane recovery of ca. 70% is identified to achieve a higher methane purity at the same cost, which may gain an economic benefit when it is operated at high plant capacity. Although the SAPO-34 membrane system is technologically feasible for the enrichment of 1.5 vol% VAM, novel membranes with a higher N2/CH4 selectivity of greater than 25 is required to reduce the membrane stages for the pre-concentration of a very diluted VAM of <1 vol%. Considering a large-scale application in the methane recovery from the coal-mining ventilation air, carbon hollow fiber membranes may have the potential to address the challenges of the high production cost and the module up-scaling with large packing density that is faced by zeolite membranes.en_US
dc.language.isoengen_US
dc.publisherElsevieren_US
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleOptimizing methane recovery: Techno-economic feasibility analysis of N2-selective membranes for the enrichment of ventilation air methaneen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionacceptedVersionen_US
dc.source.journalSeparation and Purification Technologyen_US
dc.identifier.doi10.1016/j.seppur.2020.118180
dc.identifier.cristin1857729
dc.description.localcode"© 2020. This is the authors’ accepted and refereed manuscript to the article. Locked until 9.12.2022 due to copyright restrictions. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/ "en_US
cristin.ispublishedfalse
cristin.fulltextpostprint
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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