Open AccessParticularity of Heat Exchange of Twisted Heat Exchangers in External Flow
Author(s) -
Валерій Омелянович Туз,
Nataliy Lebed,
M.P. Lytvynenko
Publication year - 2021
Publication title -
vestnik nacionalʹnogo tehničeskogo universiteta "hpi". seriâ: ènergetičeskie i teplotehničeskie processy i oborudovanie/vestnik nacionalʹnogo tehničeskogo universiteta "hpi". ènergetičeskie i teplotehničeskie processy i oborudovanie
Language(s) - English
Resource type - Journals
eISSN - 2707-7543
pISSN - 2078-774X
DOI - 10.20998/2078-774x.2021.03.02
Subject(s) - heat exchanger , laminar flow , heat transfer , mechanical engineering , plate fin heat exchanger , flow (mathematics) , mechanics , power (physics) , computer science , process engineering , nuclear engineering , plate heat exchanger , thermodynamics , engineering , physics
Perfecting the existing technologies and developing new ones require to rethink the processes in order to obtain qualitatively new results. Widespread use of cryogenic engineering in the chemical industry and medicine calls for a thorough analysis of both the efficiency of thermodynamic cycles and the hardware design of appropriate equipment. The power necessary to obtain low working medium temperatures is distributed between the cooling of the object and the losses in the various elements of the cryogenic setup. One of the best ways to increase the efficiency of the setup is to use the cold energy recovery. This is done by using various designs of recuperative heat exchangers, such as twisted heat exchangers. Existing methods of calculating the parameters of power equipment are based on empirical dependencies, which require some justification and clarification in order to be used for calculating cryogenic equipment parameters. The article describes the experimental setup, presents the research methods applied and analyses the results of the study on convective heat transfer in external flow past the tubular surface of the twisted heat exchanger. The obtained results for the laminar gas flow mode at Re < 2300 allowed determining the length of the initial heat section depending on the regime parameters of the contact phases and the geometric specifications of the twisted heat exchanger. The obtained dependence will make it possible to refine the method of calculating the parameters of the twisted heat exchanger in the annular channel.