Optimal Retrofit Strategy of Heat Exchanger Networks Applied in Crude Oil Distillation Units

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Autoren

  • Xin-Wen Liu
  • Xing Luo
  • Stephan Kabelac

Organisationseinheiten

Externe Organisationen

  • Ningbo University of Technology
Forschungs-netzwerk anzeigen

Details

OriginalspracheEnglisch
Seiten (von - bis)11283-11290
Seitenumfang8
FachzeitschriftIndustrial and Engineering Chemistry Research
Jahrgang55
Ausgabenummer43
Frühes Online-Datum21 Okt. 2016
PublikationsstatusVeröffentlicht - 2 Nov. 2016

Abstract

A novel mathematical programming method was applied to acquire the optimal heat exchanger network (HEN) retrofit in the crude oil distillation unit. The mathematical model was based on the stagewise superstructure model with splits of streams from the work of Yee et al. [Chin. J. Chem. Eng. 2007, 15 (2), 296-301]. The objective function was developed into the minimum of the sum of the cost of modifications and the cost of utilities in one year, focusing on the changing heat transfer coefficients arising in the reused existing heat exchangers from stream splits. The HEN modifications included buying new heat exchangers, adding or reducing areas of the existing heat exchangers, moving the existing heat exchangers, and laying pipes. It was a mixed integer nonlinear program (MINLP) problem. A hybrid genetic algorithm was used to optimize the MINLP problem. In order to reduce the total cost of modifications, the heat exchangers and the corresponding matching structures between the hot and cold streams in the existing HENs were designed as elites introduced into the hybrid genetic algorithm. The Dittus-Boelter and Kern correlations were used to estimate the convective heat transfer coefficients of the corresponding streams. One example was given to show the effect of the novel retrofit strategy.

Zitieren

Optimal Retrofit Strategy of Heat Exchanger Networks Applied in Crude Oil Distillation Units. / Liu, Xin-Wen; Luo, Xing; Kabelac, Stephan.
in: Industrial and Engineering Chemistry Research, Jahrgang 55, Nr. 43, 02.11.2016, S. 11283-11290.

Publikation: Beitrag in FachzeitschriftArtikelForschungPeer-Review

Liu XW, Luo X, Kabelac S. Optimal Retrofit Strategy of Heat Exchanger Networks Applied in Crude Oil Distillation Units. Industrial and Engineering Chemistry Research. 2016 Nov 2;55(43):11283-11290. Epub 2016 Okt 21. doi: 10.1021/acs.iecr.6b01931
Liu, Xin-Wen ; Luo, Xing ; Kabelac, Stephan. / Optimal Retrofit Strategy of Heat Exchanger Networks Applied in Crude Oil Distillation Units. in: Industrial and Engineering Chemistry Research. 2016 ; Jahrgang 55, Nr. 43. S. 11283-11290.
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abstract = "A novel mathematical programming method was applied to acquire the optimal heat exchanger network (HEN) retrofit in the crude oil distillation unit. The mathematical model was based on the stagewise superstructure model with splits of streams from the work of Yee et al. [Chin. J. Chem. Eng. 2007, 15 (2), 296-301]. The objective function was developed into the minimum of the sum of the cost of modifications and the cost of utilities in one year, focusing on the changing heat transfer coefficients arising in the reused existing heat exchangers from stream splits. The HEN modifications included buying new heat exchangers, adding or reducing areas of the existing heat exchangers, moving the existing heat exchangers, and laying pipes. It was a mixed integer nonlinear program (MINLP) problem. A hybrid genetic algorithm was used to optimize the MINLP problem. In order to reduce the total cost of modifications, the heat exchangers and the corresponding matching structures between the hot and cold streams in the existing HENs were designed as elites introduced into the hybrid genetic algorithm. The Dittus-Boelter and Kern correlations were used to estimate the convective heat transfer coefficients of the corresponding streams. One example was given to show the effect of the novel retrofit strategy.",
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AU - Luo, Xing

AU - Kabelac, Stephan

N1 - Publisher Copyright: © 2016 American Chemical Society. Copyright: Copyright 2017 Elsevier B.V., All rights reserved.

PY - 2016/11/2

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N2 - A novel mathematical programming method was applied to acquire the optimal heat exchanger network (HEN) retrofit in the crude oil distillation unit. The mathematical model was based on the stagewise superstructure model with splits of streams from the work of Yee et al. [Chin. J. Chem. Eng. 2007, 15 (2), 296-301]. The objective function was developed into the minimum of the sum of the cost of modifications and the cost of utilities in one year, focusing on the changing heat transfer coefficients arising in the reused existing heat exchangers from stream splits. The HEN modifications included buying new heat exchangers, adding or reducing areas of the existing heat exchangers, moving the existing heat exchangers, and laying pipes. It was a mixed integer nonlinear program (MINLP) problem. A hybrid genetic algorithm was used to optimize the MINLP problem. In order to reduce the total cost of modifications, the heat exchangers and the corresponding matching structures between the hot and cold streams in the existing HENs were designed as elites introduced into the hybrid genetic algorithm. The Dittus-Boelter and Kern correlations were used to estimate the convective heat transfer coefficients of the corresponding streams. One example was given to show the effect of the novel retrofit strategy.

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