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dc.contributor.authorBerstad, David Olsson
dc.contributor.authorAnantharaman, Rahul
dc.contributor.authorNekså, Petter
dc.date.accessioned2020-04-23T13:11:17Z
dc.date.available2020-04-23T13:11:17Z
dc.date.created2013-10-30T15:26:06Z
dc.date.issued2013
dc.identifier.citationChemical Engineering Transactions. 2013, 355-360.en_US
dc.identifier.isbn978-88-95608-26-6
dc.identifier.issn1974-9791
dc.identifier.urihttps://hdl.handle.net/11250/2652248
dc.description.abstractAs an alternative to baseline technology a low-temperature syngas separation process has been proposed for pre-combustion CO2 capture from coal-derived syngas for an IGCC plant. Through systematic process synthesis – sequencing of separators and location of compressors and expanders, followed by Pinch Analysis and energy targeting – a process design has been proposed and the net power consumption has been estimated. From a targeted power consumption of 21.9 MW the figure for the proposed design is increased to 22.9 MW mainly due to increased load for auxiliary refrigeration at low temperature. The power consumption of the proposed design represents further improvement from earlier designs that have already been shown to have higher energy efficiency than baseline technology.en_US
dc.language.isoengen_US
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleIntegrated Low-temperature CO2 Capture from IGCC Power Plant by Partial Condensation and Separation of Syngasen_US
dc.typePeer revieweden_US
dc.typeJournal articleen_US
dc.description.versionpublishedVersionen_US
dc.source.pagenumber355-360en_US
dc.source.journalChemical Engineering Transactionsen_US
dc.identifier.doi10.3303/CET1335059
dc.identifier.cristin1061703
dc.relation.projectNorges forskningsråd: 193816en_US
cristin.unitcode7548,60,0,0
cristin.unitnameGassteknologi
cristin.ispublishedtrue
cristin.fulltextoriginal
cristin.qualitycode1


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
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