Cost-Effective Reconstruction of Existing Two-Stream Heat Exchanger Systems; Theoretical Foundations of Chemical Engineering; Vol. 59, iss. 5

Detaylı Bibliyografya
Parent link:Theoretical Foundations of Chemical Engineering=Теоретические основы химической технологии.— .— New York: Pleiades Publishing, Ltd.
Vol. 59, iss. 5.— 2025.— P. 1416-1430
Müşterek Yazar: Национальный исследовательский Томский политехнический университет Исследовательская школа химических и биомедицинских технологий
Diğer Yazarlar: Uljev (Ulyev) L. M. Leonid Mikhaylovich, Gil T. A. Tatjyana Alekseevna, Norin V. V. Vladislav Vadimovich, Kuvardina E. V. Evgeniya Vyacheslavovna, Kondrashev D. O.
Özet:The paper proposes a method for optimizing a two-stream heat exchanger system, taking into account technical constraints imposed by heat exchange equipment, and the economic efficiency of the retrofit project. The optimization of the heat exchanger network is carried out considering the necessity of conducting an safety expert review in cases where process flow temperatures exceed the design temperatures of heat exchange equipment. This method was applied to optimize energy consumption at a real hydrocracking unit. Two types of heat exchange equipment are considered, specifically, shell-and-tube and plate type heat exchangers, for a possible increase in the heat transfer area within the existing heat recovery system. For shell-and-tube heat exchangers, the minimum annual cost of the retrofit project is observed at a 500 m2 increase in heat transfer area, which corresponds to the installation of a two-section heat exchanger. This enables reducing specific consumption of hot utilities by 51% and cold utilities by 31%, with a payback period of ~1.5 years. At the same time, for plate heat exchangers, the minimum annual cost is achieved at a 400 m2 increase in heat transfer area. The cost of such a retrofit project is 18% lower than that for shell-and-tube exchangers, while the reduction in specific consumption of hot and cold utilities is 66 and 40%, respectively
Текстовый файл
AM_Agreement
Dil:İngilizce
Baskı/Yayın Bilgisi: 2025
Konular:
Online Erişim:https://doi.org/10.1134/S004057952660049X
Статья на русском языке
Materyal Türü: Elektronik Kitap Bölümü
KOHA link:https://koha.lib.tpu.ru/cgi-bin/koha/opac-detail.pl?biblionumber=688673

MARC

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330 |a The paper proposes a method for optimizing a two-stream heat exchanger system, taking into account technical constraints imposed by heat exchange equipment, and the economic efficiency of the retrofit project. The optimization of the heat exchanger network is carried out considering the necessity of conducting an safety expert review in cases where process flow temperatures exceed the design temperatures of heat exchange equipment. This method was applied to optimize energy consumption at a real hydrocracking unit. Two types of heat exchange equipment are considered, specifically, shell-and-tube and plate type heat exchangers, for a possible increase in the heat transfer area within the existing heat recovery system. For shell-and-tube heat exchangers, the minimum annual cost of the retrofit project is observed at a 500 m2 increase in heat transfer area, which corresponds to the installation of a two-section heat exchanger. This enables reducing specific consumption of hot utilities by 51% and cold utilities by 31%, with a payback period of ~1.5 years. At the same time, for plate heat exchangers, the minimum annual cost is achieved at a 400 m2 increase in heat transfer area. The cost of such a retrofit project is 18% lower than that for shell-and-tube exchangers, while the reduction in specific consumption of hot and cold utilities is 66 and 40%, respectively 
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701 1 |a Gil  |b T. A.  |c Chemical engineer  |c Engineer of Tomsk Polytechnic University  |f 1997-  |g Tatjyana Alekseevna  |9 22737 
701 1 |a Norin  |b V. V.  |g Vladislav Vadimovich 
701 1 |a Kuvardina  |b E. V.  |g Evgeniya Vyacheslavovna 
701 1 |a Kondrashev  |b D. O. 
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