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dc.contributor.authorYu, Haoshui
dc.contributor.authorFu, Chao
dc.contributor.authorGundersen, Truls
dc.date.accessioned2020-01-22T07:36:20Z
dc.date.available2020-01-22T07:36:20Z
dc.date.created2018-08-14T14:13:59Z
dc.date.issued2018
dc.identifier.citationComputer-aided chemical engineering. 2018, 44 481-486.nb_NO
dc.identifier.issn1570-7946
dc.identifier.urihttp://hdl.handle.net/11250/2637361
dc.description.abstractDesign and optimization of Heat Exchanger Networks (HENs) is well established and has been heavily applied in the process industries since its pioneering period in the 1970s and 1980s. While temperature and thermal energy (heat) obviously are key elements in process plants and power stations, pressure and mechanical energy (work) are equally important. By adding expanders and compressors as equipment and power as a utility to the classical HEN problem, the considerably more challenging Work and Heat Exchange Network (WHEN) problem has been formulated as a new and growing discipline within Process Systems Engineering (PSE). Considerable opportunities exist for improving energy efficiency in process plants and power stations by using the WHEN methodology. Recent applications include (I) design of LNG processes, (II) design of CO2 capture processes, and (III) an industrial sensible heat pump. In fact, WHENs have strong similarities to Heat Pumps and Refrigeration Cycles, with the additional advantage of a PSE approach. Challenges in the graphical methodology for WHENs compared to HENs include (a) the shape of Composite and Grand Composite Curves will change with pressure manipulations, (b) the Pinch points may change, (c) the hot and cold utility demands will change, (d) the stream identity (hot or cold) may temporarily change, (e) process streams may be used as utilities, and (f) work and heat have different energy quality. To overcome the above challenges, the WHENs problem could be addressed by developing Optimization models using Total Annual Cost as the objective function. However, new challenges will appear if Mathematical Programming is used, such as (i) developing a sufficiently rich yet efficient superstructure, (ii) nonconvexities in the model that may result in local optima, (iii) potentially a large number of binary variables that may give a combinatorial explosion, and (iv) discontinuities in the process models that will cause numerical problems and slow down convergence, unless recent developments in nonsmooth analysis can be adopted for these problems. © 2018 Elsevier B.V.nb_NO
dc.language.isoengnb_NO
dc.publisherElseviernb_NO
dc.titleWork and Heat Exchange Networks – Opportunities and Challengesnb_NO
dc.typeJournal articlenb_NO
dc.typePeer reviewednb_NO
dc.description.versionpublishedVersionnb_NO
dc.source.pagenumber481-486nb_NO
dc.source.volume44nb_NO
dc.source.journalComputer-aided chemical engineeringnb_NO
dc.identifier.doi10.1016/B978-0-444-64241-7.50075-6
dc.identifier.cristin1601975
dc.relation.projectNorges forskningsråd: 257632nb_NO
dc.description.localcodeThis article will not be available due to copyright restrictions (c) 2019 by Elseviernb_NO
cristin.unitcode194,64,25,0
cristin.unitnameInstitutt for energi- og prosessteknikk
cristin.ispublishedtrue
cristin.fulltextpostprint
cristin.qualitycode1


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