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dc.contributor.authorFu, Chao
dc.contributor.authorAnantharaman, Rahul
dc.contributor.authorGundersen, Truls
dc.date.accessioned2018-03-15T09:25:28Z
dc.date.available2018-03-15T09:25:28Z
dc.date.created2015-04-09T09:58:31Z
dc.date.issued2015
dc.identifier.citationEnergy. 2015, 84 612-622.nb_NO
dc.identifier.issn0360-5442
dc.identifier.urihttp://hdl.handle.net/11250/2490648
dc.description.abstractThe integration of process heat with regenerative steam Rankine cycles by preheating the boiler feedwater increases power generation from the steam turbines. In oxy-combustion coal based power plants, considerable compression heat from the air separation unit is available for such heat integration, however, there are at least two challenges: (1) how to integrate a heat stream with the steam cycle, and (2) how to optimize the compression scheme, accounting for the trade-off between compression work requirement and the turbine power output. This paper investigates the optimal integration of the air compression train in a cryogenic air separation unit with the regenerative steam cycle in an oxy-combustion coal based power plant using MINLP (mixed Integer non-linear programming) Two special cases (adiabatic compression and “isothermal” compression) are also investigated to compare with the optimization results. The study shows that such heat integration increases the thermal efficiency of the reference power plant by a maximum of 0.5–0.6% points. The heat integration is less attractive when the temperature difference of the heat transfer between the compressed gas and the boiler feedwater is larger than 40 °C.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.rightsAttribution-NonCommercial-NoDerivatives 4.0 Internasjonal*
dc.rights.urihttp://creativecommons.org/licenses/by-nc-nd/4.0/deed.no*
dc.titleOptimal integration of compression heat with regenerative steam Rankine cycles in oxy-combustion coal based power plantsnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionacceptedVersionnb_NO
dc.source.pagenumber612-622nb_NO
dc.source.volume84nb_NO
dc.source.journalEnergynb_NO
dc.identifier.doi10.1016/j.energy.2015.03.023
dc.identifier.cristin1236178
dc.relation.projectNorges forskningsråd: 193816nb_NO
dc.description.localcode© 2015. This is the authors’ accepted and refereed manuscript to the article. This manuscript version is made available under the CC-BY-NC-ND 4.0 license http://creativecommons.org/licenses/by-nc-nd/4.0/nb_NO
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode2


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Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal
Except where otherwise noted, this item's license is described as Attribution-NonCommercial-NoDerivatives 4.0 Internasjonal