Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot

This paper presents a systematic technique to select the optimal design target for the heat exchanger network (HEN) synthesis by using a new trade-off plot which considers aspects of design, controllability in terms of steady state flexibility and sensitivity analysis, and cost. By selecting the HEN...

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Main Authors: Abu Bakar, Suraya Hanim, Abd. Hamid, Mohd. Kamaruddin, Wan Alwi, Sharifah Rafidah, Abdul Manan, Zainuddin
Format: Article
Published: Elsevier Ltd 2016
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Online Access:http://eprints.utm.my/id/eprint/73965/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84940061385&doi=10.1016%2fj.apenergy.2015.07.056&partnerID=40&md5=466964c1dc85f7928138c7b0661d58ae
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spelling my.utm.739652017-11-23T01:37:07Z http://eprints.utm.my/id/eprint/73965/ Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot Abu Bakar, Suraya Hanim Abd. Hamid, Mohd. Kamaruddin Wan Alwi, Sharifah Rafidah Abdul Manan, Zainuddin TP Chemical technology This paper presents a systematic technique to select the optimal design target for the heat exchanger network (HEN) synthesis by using a new trade-off plot which considers aspects of design, controllability in terms of steady state flexibility and sensitivity analysis, and cost. By selecting the HEN design target according to this guideline, the designer is able to predict the design, operability, and controllability of the designed HEN at the beginning of the synthesis stage. In this study, the HEN design target that needs to be optimized is the value of the minimum temperature difference (δTmin). In traditional HEN synthesis, designers only consider the trade-off between capital and operating costs in selecting the best δTmin. As a result, the HEN design at the selected δTmin may not be optimum in terms of steady state controllability. In addition to considering the capital and operating costs, the proposed new method provides additional design insights in terms of energy recovery, operability, controllability (steady state) through the flexibility and sensitivity. The proposed trade-off plot allows designers to choose the most suitable design target either for the purpose of improving a network's energy recovery and/or controllability. A case study has been applied to test the capability of the new proposed trade-off plot. The results show that δTmin = 40 °C is the optimal design target to synthesize flexible and operable HEN. Elsevier Ltd 2016 Article PeerReviewed Abu Bakar, Suraya Hanim and Abd. Hamid, Mohd. Kamaruddin and Wan Alwi, Sharifah Rafidah and Abdul Manan, Zainuddin (2016) Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot. Applied Energy, 162 . pp. 1259-1271. ISSN 0306-2619 https://www.scopus.com/inward/record.uri?eid=2-s2.0-84940061385&doi=10.1016%2fj.apenergy.2015.07.056&partnerID=40&md5=466964c1dc85f7928138c7b0661d58ae
institution Universiti Teknologi Malaysia
building UTM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Malaysia
content_source UTM Institutional Repository
url_provider http://eprints.utm.my/
topic TP Chemical technology
spellingShingle TP Chemical technology
Abu Bakar, Suraya Hanim
Abd. Hamid, Mohd. Kamaruddin
Wan Alwi, Sharifah Rafidah
Abdul Manan, Zainuddin
Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
description This paper presents a systematic technique to select the optimal design target for the heat exchanger network (HEN) synthesis by using a new trade-off plot which considers aspects of design, controllability in terms of steady state flexibility and sensitivity analysis, and cost. By selecting the HEN design target according to this guideline, the designer is able to predict the design, operability, and controllability of the designed HEN at the beginning of the synthesis stage. In this study, the HEN design target that needs to be optimized is the value of the minimum temperature difference (δTmin). In traditional HEN synthesis, designers only consider the trade-off between capital and operating costs in selecting the best δTmin. As a result, the HEN design at the selected δTmin may not be optimum in terms of steady state controllability. In addition to considering the capital and operating costs, the proposed new method provides additional design insights in terms of energy recovery, operability, controllability (steady state) through the flexibility and sensitivity. The proposed trade-off plot allows designers to choose the most suitable design target either for the purpose of improving a network's energy recovery and/or controllability. A case study has been applied to test the capability of the new proposed trade-off plot. The results show that δTmin = 40 °C is the optimal design target to synthesize flexible and operable HEN.
format Article
author Abu Bakar, Suraya Hanim
Abd. Hamid, Mohd. Kamaruddin
Wan Alwi, Sharifah Rafidah
Abdul Manan, Zainuddin
author_facet Abu Bakar, Suraya Hanim
Abd. Hamid, Mohd. Kamaruddin
Wan Alwi, Sharifah Rafidah
Abdul Manan, Zainuddin
author_sort Abu Bakar, Suraya Hanim
title Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
title_short Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
title_full Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
title_fullStr Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
title_full_unstemmed Selection of minimum temperature difference (dTmin) for heat exchanger network synthesis based on trade-off plot
title_sort selection of minimum temperature difference (dtmin) for heat exchanger network synthesis based on trade-off plot
publisher Elsevier Ltd
publishDate 2016
url http://eprints.utm.my/id/eprint/73965/
https://www.scopus.com/inward/record.uri?eid=2-s2.0-84940061385&doi=10.1016%2fj.apenergy.2015.07.056&partnerID=40&md5=466964c1dc85f7928138c7b0661d58ae
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