MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train

There is greater awareness today on the depleting fossil energy resources and the growing problem of atmospheric pollution. Engineers are developing practical techniques to ensure energy processes are designed and operated efficiently. Inefficient heat exchangers lead to higher fuel demand and hig...

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Main Authors: Zulkafli, Nur Izyan, Mahadzir, Shuhaimi, Hashim, Haslenda
Format: Conference or Workshop Item
Language:English
Published: 2013
Subjects:
Online Access:http://eprints.utem.edu.my/id/eprint/10538/1/PSEAsia2013-80.pdf
http://eprints.utem.edu.my/id/eprint/10538/
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Institution: Universiti Teknikal Malaysia Melaka
Language: English
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spelling my.utem.eprints.105382015-05-28T04:11:47Z http://eprints.utem.edu.my/id/eprint/10538/ MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train Zulkafli, Nur Izyan Mahadzir, Shuhaimi Hashim, Haslenda T Technology (General) QA Mathematics TA Engineering (General). Civil engineering (General) There is greater awareness today on the depleting fossil energy resources and the growing problem of atmospheric pollution. Engineers are developing practical techniques to ensure energy processes are designed and operated efficiently. Inefficient heat exchangers lead to higher fuel demand and higher carbon emission. This paper presents mixed-integer nonlinear programming (MINLP) model for simultaneous cleaning and retrofit of crude preheat train (CPT) in oil refinery plant. The formulation of the model is generated and coded in General Algebraic Modeling System (GAMS). The model minimizes the cost of energy and the cost of cleaning. The model takes into account the changes in fouling rates throughout time. There are two cases for this study. The cases are online cleaning (Case 1) and simultaneous online cleaning and retrofit (Case 2). The largest energy saving are found in Case 2. The installation of high efficiency heat exchangers improves furnace inlet temperature (FIT) from 215oC to 227oC. Furthermore, Case 2 results in the highest percentage of cost saving by about 59%. The payback period for investment in high efficiency heat exchangers is 5 months. Thus, Case 2 is the most cost effective option for reductions of energy consumption in Crude Distillation Unit (CDU). 2013-06-25 Conference or Workshop Item PeerReviewed application/pdf en http://eprints.utem.edu.my/id/eprint/10538/1/PSEAsia2013-80.pdf Zulkafli, Nur Izyan and Mahadzir, Shuhaimi and Hashim, Haslenda (2013) MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train. In: 6th International Conference on Process System Engineering 2013 (PSE Asia 2013), 25-27 June 2013, PWTC, Kuala Lumpur, Malaysia. (Unpublished)
institution Universiti Teknikal Malaysia Melaka
building UTEM Library
collection Institutional Repository
continent Asia
country Malaysia
content_provider Universiti Teknikal Malaysia Melaka
content_source UTEM Institutional Repository
url_provider http://eprints.utem.edu.my/
language English
topic T Technology (General)
QA Mathematics
TA Engineering (General). Civil engineering (General)
spellingShingle T Technology (General)
QA Mathematics
TA Engineering (General). Civil engineering (General)
Zulkafli, Nur Izyan
Mahadzir, Shuhaimi
Hashim, Haslenda
MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
description There is greater awareness today on the depleting fossil energy resources and the growing problem of atmospheric pollution. Engineers are developing practical techniques to ensure energy processes are designed and operated efficiently. Inefficient heat exchangers lead to higher fuel demand and higher carbon emission. This paper presents mixed-integer nonlinear programming (MINLP) model for simultaneous cleaning and retrofit of crude preheat train (CPT) in oil refinery plant. The formulation of the model is generated and coded in General Algebraic Modeling System (GAMS). The model minimizes the cost of energy and the cost of cleaning. The model takes into account the changes in fouling rates throughout time. There are two cases for this study. The cases are online cleaning (Case 1) and simultaneous online cleaning and retrofit (Case 2). The largest energy saving are found in Case 2. The installation of high efficiency heat exchangers improves furnace inlet temperature (FIT) from 215oC to 227oC. Furthermore, Case 2 results in the highest percentage of cost saving by about 59%. The payback period for investment in high efficiency heat exchangers is 5 months. Thus, Case 2 is the most cost effective option for reductions of energy consumption in Crude Distillation Unit (CDU).
format Conference or Workshop Item
author Zulkafli, Nur Izyan
Mahadzir, Shuhaimi
Hashim, Haslenda
author_facet Zulkafli, Nur Izyan
Mahadzir, Shuhaimi
Hashim, Haslenda
author_sort Zulkafli, Nur Izyan
title MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
title_short MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
title_full MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
title_fullStr MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
title_full_unstemmed MINLP Model for Simultaneous Scheduling and Retrofit of Refinery Preheat Train
title_sort minlp model for simultaneous scheduling and retrofit of refinery preheat train
publishDate 2013
url http://eprints.utem.edu.my/id/eprint/10538/1/PSEAsia2013-80.pdf
http://eprints.utem.edu.my/id/eprint/10538/
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