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dc.contributor.authorLi, Hailong
dc.contributor.authorTan, Y
dc.contributor.authorDitaranto, Mario
dc.contributor.authorYan, Jinying
dc.contributor.authorYu, Zhixin
dc.date.accessioned2021-08-19T09:15:49Z
dc.date.available2021-08-19T09:15:49Z
dc.date.created2017-08-21T13:45:21Z
dc.date.issued2017-07
dc.identifier.citationLi, H., Tan, Y., Ditaranto, M. et al. (2017) Capturing CO2 from Biogas Plants. Energy Procedia, 114, pp. 6030-6035.en_US
dc.identifier.issn1876-6102
dc.identifier.urihttps://hdl.handle.net/11250/2770246
dc.description.abstractAs a renewable energy, biogas produced from anaerobic digestion and landfill is playing a more and more important role in the energy market. Capturing CO2 from biogas can result in a negative CO2 emission. Depending on how biogas is utilized, there are different routes to capture CO2. A biogas plant that uses raw biogas to produce power and heat can be retrofitted by integrating CO2 capture. In order to identify the best option, three retrofits were compared from both technical and economic perspectives, including SYS-I, which captures CO2 from raw gas and produces biomethane instead of electricity and heat, SYS-II, which captures CO2 using MEA-based chemical absorption after the combustion of raw gas, and SYS-III, which captures CO2 by using oxy-fuel combustion of the raw gas. In general, SYS-I can achieve the highest profit and shortest payback time, mainly due to the high price of biomethane. SYSII and SYS-III are clearly influenced by carbon credit. In order to have positive profits for the retrofits of SYS-II and SYS-III, carbon credit needs to exceed 750SEK (or 100USD)/ton CO2 and 113 SEK (or 15USD)/ton CO2 respectively.en_US
dc.language.isoengen_US
dc.publisherElsevier Ltd.en_US
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.subjectkarbonfangsten_US
dc.subjectbiogassen_US
dc.titleCapturing CO2 from Biogas Plantsen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.rights.holder© 2017 The Authors.en_US
dc.subject.nsiVDP::Teknologi: 500en_US
dc.subject.nsiVDP::Matematikk og Naturvitenskap: 400::Basale biofag: 470en_US
dc.source.pagenumber6030-6035en_US
dc.source.volume114en_US
dc.source.journalEnergy Procediaen_US
dc.identifier.doi10.1016/j.egypro.2017.03.1738
dc.identifier.cristin1487653
dc.relation.projectNorges forskningsråd: 193816en_US
cristin.unitcode217,8,6,0
cristin.unitnameInstitutt for petroleumsteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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