Приказ основних података о документу

dc.creatorMontolio-Rodriguez, Daniel
dc.creatorLinke, Patrick
dc.creatorLinke, David
dc.creatorStijepović, Mirko
dc.date.accessioned2021-03-10T11:24:36Z
dc.date.available2021-03-10T11:24:36Z
dc.date.issued2010
dc.identifier.issn1385-8947
dc.identifier.urihttp://TechnoRep.tmf.bg.ac.rs/handle/123456789/1724
dc.description.abstractThis paper presents an optimisation-based method for the screening and conceptual design of processes with heterogeneous catalytic reactors. The method follows a multi-level approach to process synthesis to establish performance targets and identify high-performance designs. At each level, process superstructures are optimised to explore performance limits of the system and to guide the understanding of the relationships between individual design features and process performance. This enables the design engineer to explore trade-offs between performance and structural complexity in a coordinated manner. The method leads to a number of potential design candidates that provide the design engineers with insight into the performance gains that can be expected by increasing design complexity. The method has been developed and implemented for heterogeneously catalysed gas-phase reaction systems and is illustrated with an example in styrene production.en
dc.publisherElsevier Science Sa, Lausanne
dc.rightsrestrictedAccess
dc.sourceChemical Engineering Journal
dc.subjectReaction engineeringen
dc.subjectProcess synthesisen
dc.subjectHeterogeneous catalysisen
dc.subjectSuperstructure optimisationen
dc.subjectStyreneen
dc.titleOptimal conceptual design of processes with heterogeneous catalytic reactorsen
dc.typearticle
dc.rights.licenseARR
dc.citation.epage449
dc.citation.issue3
dc.citation.other163(3): 438-449
dc.citation.rankaM21
dc.citation.spage438
dc.citation.volume163
dc.identifier.doi10.1016/j.cej.2010.08.006
dc.identifier.scopus2-s2.0-77956650244
dc.identifier.wos000283449400034
dc.type.versionpublishedVersion


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Приказ основних података о документу