Exergy analysis for fuel reduction strategies in crude distillation unit

Inefficient furnaces and heat exchangers contribute to the depletion of fossil fuel problem due to higher fuel demand and higher carbon emission. The method of exergy analysis is applied to the furnace and crude preheat train (CPT) in a crude distillation unit (CDU) to determine performance benchmar...

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Main Authors: Izyan, Z.N., Shuhaimi, M.
Format: Article
Published: Elsevier Ltd 2014
Online Access:https://www.scopus.com/inward/record.uri?eid=2-s2.0-84896404211&doi=10.1016%2fj.energy.2014.01.026&partnerID=40&md5=21b28264e21f2b39ee81c682927644f6
http://eprints.utp.edu.my/31341/
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spelling my.utp.eprints.313412022-03-25T09:06:26Z Exergy analysis for fuel reduction strategies in crude distillation unit Izyan, Z.N. Shuhaimi, M. Inefficient furnaces and heat exchangers contribute to the depletion of fossil fuel problem due to higher fuel demand and higher carbon emission. The method of exergy analysis is applied to the furnace and crude preheat train (CPT) in a crude distillation unit (CDU) to determine performance benchmark of the system. This paper presents exergy analysis and strategies to reduce exergy loss through process modification. The highest exergy loss was found to be located at the inlet furnace. The proposed options for fuel reduction strategies are reduction of heat loss from furnace stack and overall cleaning schedule of CPT. The feasibility and economic analysis for both options are investigated. From the results, overall cleaning schedule of CPT contributes to the highest energy saving of 5.6. However, reduction of heat loss from furnace stack is the highest cost saving by about 6.4. © 2014 Elsevier Ltd. Elsevier Ltd 2014 Article NonPeerReviewed https://www.scopus.com/inward/record.uri?eid=2-s2.0-84896404211&doi=10.1016%2fj.energy.2014.01.026&partnerID=40&md5=21b28264e21f2b39ee81c682927644f6 Izyan, Z.N. and Shuhaimi, M. (2014) Exergy analysis for fuel reduction strategies in crude distillation unit. Energy, 66 . pp. 891-897. http://eprints.utp.edu.my/31341/
institution Universiti Teknologi Petronas
building UTP Resource Centre
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknologi Petronas
content_source UTP Institutional Repository
url_provider http://eprints.utp.edu.my/
description Inefficient furnaces and heat exchangers contribute to the depletion of fossil fuel problem due to higher fuel demand and higher carbon emission. The method of exergy analysis is applied to the furnace and crude preheat train (CPT) in a crude distillation unit (CDU) to determine performance benchmark of the system. This paper presents exergy analysis and strategies to reduce exergy loss through process modification. The highest exergy loss was found to be located at the inlet furnace. The proposed options for fuel reduction strategies are reduction of heat loss from furnace stack and overall cleaning schedule of CPT. The feasibility and economic analysis for both options are investigated. From the results, overall cleaning schedule of CPT contributes to the highest energy saving of 5.6. However, reduction of heat loss from furnace stack is the highest cost saving by about 6.4. © 2014 Elsevier Ltd.
format Article
author Izyan, Z.N.
Shuhaimi, M.
spellingShingle Izyan, Z.N.
Shuhaimi, M.
Exergy analysis for fuel reduction strategies in crude distillation unit
author_facet Izyan, Z.N.
Shuhaimi, M.
author_sort Izyan, Z.N.
title Exergy analysis for fuel reduction strategies in crude distillation unit
title_short Exergy analysis for fuel reduction strategies in crude distillation unit
title_full Exergy analysis for fuel reduction strategies in crude distillation unit
title_fullStr Exergy analysis for fuel reduction strategies in crude distillation unit
title_full_unstemmed Exergy analysis for fuel reduction strategies in crude distillation unit
title_sort exergy analysis for fuel reduction strategies in crude distillation unit
publisher Elsevier Ltd
publishDate 2014
url https://www.scopus.com/inward/record.uri?eid=2-s2.0-84896404211&doi=10.1016%2fj.energy.2014.01.026&partnerID=40&md5=21b28264e21f2b39ee81c682927644f6
http://eprints.utp.edu.my/31341/
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score 13.211869