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Heat exchanger network design using plate heat exchanger

Başlık çevirisi mevcut değil.

  1. Tez No: 401433
  2. Yazar: MERVE KORUYAN
  3. Danışmanlar: DR. SIMON PERRY
  4. Tez Türü: Yüksek Lisans
  5. Konular: Kimya Mühendisliği, Chemical Engineering
  6. Anahtar Kelimeler: Belirtilmemiş.
  7. Yıl: 2013
  8. Dil: İngilizce
  9. Üniversite: The University of Manchester
  10. Enstitü: Yurtdışı Enstitü
  11. Ana Bilim Dalı: Belirtilmemiş.
  12. Bilim Dalı: Belirtilmemiş.
  13. Sayfa Sayısı: 84

Özet

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Özet (Çeviri)

Heat exchanger network is an important element of chemical processes, as it improves the energy efficiency by recovering waste heat. Hereby, the operating cost can be reduced and overall plant economics is improved. The shell and tube (S&T) type is the most commonly used heat exchanger in the heat exchanger network (HEN). Using plate type heat exchanger is an alternative way in the heat exchanger network. This is because it raises the process heat recovery based on their low minimum temperature difference approach and enhanced overall heat transfer coefficient. However, recent developments in plate type heat exchangers have provided understanding about their design and performance and less information is known about their potential application in the design of heat exchanger networks. Based on the understanding of the contexts in which plate heat exchangers offer benefits, models of plate heat exchangers will be applied for design of HEN. The overall aim of this project is to expand the existing heat exchanger network design methodology (pinch design methodology) by considering plate type heat exchangers together with other design options. The SPRINT software will be utilized for synthesising HEN. Different types of plate heat exchangers have been analysed in terms of operating conditions (the temperature and pressure) and effectiveness. The present dissertation is concentrated on welded-plate and frame heat exchangers, which are suitable for high temperature and pressure (500 and 80 bar). The study findings show that integrating welded plate heat exchanger instead of a shell and tube heat exchanger provides heat recovery advantages regarding lower minimum temperature approach. When the amount of heat recovery is increased, the required external utility is decreased (operating cost is reduced). Furthermore, even a heat exchanger network that is designed by using welded-plate heat exchanger for 1 minimum approach temperature has lower capital cost than the heat exchanger network that is designed by using shell and tube heat exchanger for 15 minimum approach temperature for the same duty.

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