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dc.contributor.authorBredström, David
dc.contributor.authorFlisberg, Patrik
dc.contributor.authorRönnqvist, Mikael
dc.date.accessioned2009-04-01T10:47:27Z
dc.date.available2009-04-01T10:47:27Z
dc.date.issued2008-11
dc.identifier.isbn978-82-491-0603-5 (elektronisk versjon)
dc.identifier.isbn978-82-491-0602-8 (trykt versjon)
dc.identifier.issn0803-4036
dc.identifier.urihttp://hdl.handle.net/11250/165031
dc.description.abstractIn this paper we present a general model and solution approach for refinery process planning. The model is nonlinear and has a flexible description to account for different configurations at a refinery. The solution approach is based on solving the nonlinear model directly with a commercial solver. Since the model is highly nonlinear we apply a special procedure to find a good starting solution. We test standard commercial nonlinear solvers on a set of standard test examples.en
dc.language.isoengen
dc.publisherSNFen
dc.relation.ispartofseriesReporten
dc.relation.ispartofseries2008:24en
dc.titleRefinery production planning : model and solution methoden
dc.typeResearch reporten
dc.subject.nsiVDP::Samfunnsvitenskap: 200::Økonomi: 210::Bedriftsøkonomi: 213en
dc.subject.nsiVDP::Teknologi: 500::Berg? og petroleumsfag: 510::Petroleumsteknologi: 512en


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