Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils

Energy management is an important portion of controlling total operating costs for refineries throughout the world. For refinery, the crude distillation unit is one of the largest energy consumption units and also represents one of the most important areas for doing heat integration. The heat exchan...

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Main Authors: B. Yimyam, K. Siemanond
Format: Article
Language:English
Published: AIDIC Servizi S.r.l. 2012-09-01
Series:Chemical Engineering Transactions
Online Access:https://www.cetjournal.it/index.php/cet/article/view/7050
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spelling doaj-f352a773c66248ae9e28aa4913f6a5c32021-02-22T21:05:04ZengAIDIC Servizi S.r.l.Chemical Engineering Transactions2283-92162012-09-012910.3303/CET1229054Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude OilsB. YimyamK. SiemanondEnergy management is an important portion of controlling total operating costs for refineries throughout the world. For refinery, the crude distillation unit is one of the largest energy consumption units and also represents one of the most important areas for doing heat integration. The heat exchanger network (HEN) of crude distillation units (CDU) can be retrofitted to reduce the utility consumption. This research used the retrofit potential program, Supachai (2011) to find the optimum point in targeting step and then a mathematical programming model using General Algebraic Modelling System (GAMS) called the stage model, using the mixed integer linear programming (MILP) of Yee and Grossmann (1990) was applied to develop the retrofit model and the simulation software (PROII) was used to validate the design and to perform the total utility consumption. With using the existing exchangers, the retrofit model with the exchanger relocation technique is applied. Example problems of HEN for a crude distillation unit with light, medium and heavy crude oil feeds for a period of 100, 150 and 100 days per year, respectively, were used to demonstrate the retrofitting with the aim of finding the optimal design that would yield the highest net present value (NPV).https://www.cetjournal.it/index.php/cet/article/view/7050
collection DOAJ
language English
format Article
sources DOAJ
author B. Yimyam
K. Siemanond
spellingShingle B. Yimyam
K. Siemanond
Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
Chemical Engineering Transactions
author_facet B. Yimyam
K. Siemanond
author_sort B. Yimyam
title Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
title_short Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
title_full Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
title_fullStr Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
title_full_unstemmed Retrofit with Exchanger Relocation of Crude Preheat Train under Different Kinds of Crude Oils
title_sort retrofit with exchanger relocation of crude preheat train under different kinds of crude oils
publisher AIDIC Servizi S.r.l.
series Chemical Engineering Transactions
issn 2283-9216
publishDate 2012-09-01
description Energy management is an important portion of controlling total operating costs for refineries throughout the world. For refinery, the crude distillation unit is one of the largest energy consumption units and also represents one of the most important areas for doing heat integration. The heat exchanger network (HEN) of crude distillation units (CDU) can be retrofitted to reduce the utility consumption. This research used the retrofit potential program, Supachai (2011) to find the optimum point in targeting step and then a mathematical programming model using General Algebraic Modelling System (GAMS) called the stage model, using the mixed integer linear programming (MILP) of Yee and Grossmann (1990) was applied to develop the retrofit model and the simulation software (PROII) was used to validate the design and to perform the total utility consumption. With using the existing exchangers, the retrofit model with the exchanger relocation technique is applied. Example problems of HEN for a crude distillation unit with light, medium and heavy crude oil feeds for a period of 100, 150 and 100 days per year, respectively, were used to demonstrate the retrofitting with the aim of finding the optimal design that would yield the highest net present value (NPV).
url https://www.cetjournal.it/index.php/cet/article/view/7050
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