Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations

This paper presents a systematic synthesis method that considers multiple shells and logarithmic mean temperature difference (LMTD) FT correction factor for heat exchanger networks (HENs) involving multiple periods of operation. The approach adopted entails firstly generating a reduced multiperiod H...

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Autores principales: Adeniyi Jide Isafiade, Michael Short
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Publicado: AIDIC Servizi S.r.l. 2021
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spelling oai:doaj.org-article:2294209429484bf4a25b35b49d70a5aa2021-11-15T21:47:57ZSynthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations10.3303/CET21881092283-9216https://doaj.org/article/2294209429484bf4a25b35b49d70a5aa2021-11-01T00:00:00Zhttps://www.cetjournal.it/index.php/cet/article/view/11902https://doaj.org/toc/2283-9216This paper presents a systematic synthesis method that considers multiple shells and logarithmic mean temperature difference (LMTD) FT correction factor for heat exchanger networks (HENs) involving multiple periods of operation. The approach adopted entails firstly generating a reduced multiperiod HEN superstructure using network solutions obtained when the STEP (Stream Temperature Versus Enthalpy Plot) and HEAT (Heat Allocation and Targeting) synthesis methods are applied to each subperiod. The second stage entails generating an initial multiperiod HEN solution from the reduced superstructure synthesis approach. The number of shells, as well as the FT correction factor, required by each exchanger in each period of the initial multiperiod HEN are then manually calculated and used to initialise the multiperiod HEN to obtain updated representative heat exchanger areas for all stream pairs in all periods of operations. The solution obtained, when the method of this paper is applied to a literature example, shows that the assumption of 1 – 1 (1 shell pass – 1 tube pass) design configuration for multiperiod HEN problems, underestimates the representative heat exchanger areas by 12.3%.Adeniyi Jide IsafiadeMichael ShortAIDIC Servizi S.r.l.articleChemical engineeringTP155-156Computer engineering. Computer hardwareTK7885-7895ENChemical Engineering Transactions, Vol 88 (2021)
institution DOAJ
collection DOAJ
language EN
topic Chemical engineering
TP155-156
Computer engineering. Computer hardware
TK7885-7895
spellingShingle Chemical engineering
TP155-156
Computer engineering. Computer hardware
TK7885-7895
Adeniyi Jide Isafiade
Michael Short
Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
description This paper presents a systematic synthesis method that considers multiple shells and logarithmic mean temperature difference (LMTD) FT correction factor for heat exchanger networks (HENs) involving multiple periods of operation. The approach adopted entails firstly generating a reduced multiperiod HEN superstructure using network solutions obtained when the STEP (Stream Temperature Versus Enthalpy Plot) and HEAT (Heat Allocation and Targeting) synthesis methods are applied to each subperiod. The second stage entails generating an initial multiperiod HEN solution from the reduced superstructure synthesis approach. The number of shells, as well as the FT correction factor, required by each exchanger in each period of the initial multiperiod HEN are then manually calculated and used to initialise the multiperiod HEN to obtain updated representative heat exchanger areas for all stream pairs in all periods of operations. The solution obtained, when the method of this paper is applied to a literature example, shows that the assumption of 1 – 1 (1 shell pass – 1 tube pass) design configuration for multiperiod HEN problems, underestimates the representative heat exchanger areas by 12.3%.
format article
author Adeniyi Jide Isafiade
Michael Short
author_facet Adeniyi Jide Isafiade
Michael Short
author_sort Adeniyi Jide Isafiade
title Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
title_short Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
title_full Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
title_fullStr Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
title_full_unstemmed Synthesis of Multiperiod Heat Exchanger Networks Involving 1 Shell Pass – 2 Tube Pass Design Configurations
title_sort synthesis of multiperiod heat exchanger networks involving 1 shell pass – 2 tube pass design configurations
publisher AIDIC Servizi S.r.l.
publishDate 2021
url https://doaj.org/article/2294209429484bf4a25b35b49d70a5aa
work_keys_str_mv AT adeniyijideisafiade synthesisofmultiperiodheatexchangernetworksinvolving1shellpass2tubepassdesignconfigurations
AT michaelshort synthesisofmultiperiodheatexchangernetworksinvolving1shellpass2tubepassdesignconfigurations
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