HEN optimizations without using logarithmic-mean-temperature difference

dc.contributor.authorAkman, U
dc.contributor.authorUygun, K
dc.contributor.authorUztürk, D
dc.contributor.authorKonukman, Alp Er Şevki
dc.date.accessioned2025-10-29T11:34:34Z
dc.date.issued2002
dc.departmentFakülteler, Temel Bilimler Fakültesi, Kimya Bölümü
dc.departmentFakülteler, Mühendislik Fakültesi, Makine Mühendisliği Bölümü
dc.description.abstractA simple 1-1 shell-and-tube heat-exchanger model without the logarithmic-mean temperature difference DeltaT(lm) is proposed for heat-exchanger network (HEN) optimizations. The model consists of two algebraic equations and allows to determine hot and cold outlet temperatures independent of each other. HEN optimization problems are classified as feasible- and infeasible-path formulations, and compared with regard to problems originating from the use of DeltaT(lm) in exhanger energy-balance equations. The DeltaT(lm)-free model eliminates numerical failures in computing the logarithmic terms with negative arguments due to possible inconsistent initialization/progress of exchanger interconnection temperatures dining HEN optimizations. The DeltaT(lm)-free model does not require inclusion of approach-temperature inequality constraints since positive approach temperatures are guaranteed. It also eliminates iterative solution of nonlinear energy-balance equations in feasible-path formulations and is represented as linear equality constraints in infeasible-path formulations for fixed areas, heat-capacity-flow rates, and bypass flows. As demonstrated with two representative HEN optimization problems, the DeltaT(lm)-free model significantly reduces numerical difficulties and decreases computation time in the optimization phase of synthesis/design, retrofit, and flexibility-analysis of HENs. Thus, it permits handling large HEN problems.
dc.identifier.doi10.1002/aic.690480316
dc.identifier.endpage606
dc.identifier.issn0001-1541
dc.identifier.issue3
dc.identifier.orcid0000-0001-9440-7394
dc.identifier.scopus2-s2.0-0036489392
dc.identifier.scopusqualityQ1
dc.identifier.startpage596
dc.identifier.urihttps://doi.org/10.1002/aic.690480316
dc.identifier.urihttps://hdl.handle.net/20.500.14854/12942
dc.identifier.volume48
dc.identifier.wosWOS:000174331600015
dc.identifier.wosqualityQ1
dc.indekslendigikaynakWeb of Science
dc.indekslendigikaynakScopus
dc.language.isoen
dc.publisherWiley-Blackwell
dc.relation.ispartofAiche Journal
dc.relation.publicationcategoryMakale - Uluslararası Hakemli Dergi - Kurum Öğretim Elemanı
dc.rightsinfo:eu-repo/semantics/closedAccess
dc.snmzKA_WOS_20251020
dc.subjectHeat-Exchanger Networks
dc.subjectChemical Process Design
dc.subjectFlexibility Analysis
dc.subjectSystems
dc.subjectReplacement
dc.subjectIntegration
dc.subjectGeneration
dc.subjectModels
dc.titleHEN optimizations without using logarithmic-mean-temperature difference
dc.typeArticle

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