Engineering Journal: Science and InnovationELECTRONIC SCIENCE AND ENGINEERING PUBLICATION
Certificate of Registration Media number Эл #ФС77-53688 of 17 April 2013. ISSN 2308-6033. DOI 10.18698/2308-6033
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Article

Heat transfer intensification inhelium plant assemblies

Published: 20.06.2017

Authors: Smorodin A.I., Frolov I.A.

Published in issue: #6(66)/2017

DOI: 10.18698/2308-6033-2017-6-1658

Category: Power, Metallurgic and Chemical Engineering | Chapter: Machines and Devices, Processes of Refrigeration and Cryogenic Engineering, Air Conditioning

Russian cryogenic helium plants feature helical-coil heat exchangers made of copper tubes ribbed with copper wire, so that the heat exchanger surface becomes statistically homogeneous. This structure the right conditions to distribute the flow evenly in the heat exchange annulus. Low parallel flow pressure in KGU-5000/4,5 and a related decrease in heat transfer coefficient in the annulus made us search for possible ways of intensifying heat transfer in the pipe without increasing the size and mass of heat exchangers. We analysed the works of R. Koch and E.K. Kalinin, which lead us to selecting intensifier shape and dimensions so that they look like smoothly outlined ridges. Studies of four test heat exchangers made of wire-ribbed tubes manufactured with and without intensifiers confirmed the technological feasibility of producing a tube-based helical-coil heat exchanger out of tubes ribbed with wire, with internal intensifiers in the shape of smoothly outlined ring-shaped ridges. We determined that the heat transfer coefficient inside tubes with intensifiers is approximately twice as high as that in a smooth tube under comparable conditions. We managed to decrease the size and dimensions of these heat exchangers to install them in a large helium plant.


References
[1] Krasnikova O.K. Vitye teploobmennye apparaty kriogennykh i teploenergeticheskikh ustanovok [Helical-coil heat exchangers in cryogenic and thermal engineering plants]. Moscow, KolosS Publ., 2008, 176 p.
[2] Krasnikova O.K., Popov O.M., Udut V.N. Khimicheskoe i neftegazovoe mashinostroenie - Chemical and Petroleum Engineering, 1999, no. 9, p. 15.
[3] Krasnikova O.K., Mischenko T.S., Komarova L.R., Popov O.M., Udut V.N. Khimicheskoe i neftegazovoe mashinostroenie - Chemical and Petroleum Engineering, 2002, no. 3, pp. 32-33.
[4] Belyakov V.P., Pronko V.G., Epifanova V.I., Krasnikova O.K., Nikitkin V.D., Mischenko T.S. Trubchatyy spiralnyy teploobmennik [Tubular spiral heat exchanger]. Certific. of authorship 542902 SSSR, Intern. class. of invent. F28D7/02. no.1871186/06, USSR, newsletter no. 2, 1973, 4 p.
[5] Krasnikova O.K. Sposoby intensifikatsii teploobmena pri vynuzhdennoy konvektsii v apparatakh kriogennykh sistem [Ways of heat transfer intensification for the case of forced convection in cryogenic system assemblies]. Moscow, Central Institute of Scientific and Technical Information on Chemical and Petroleum Machinery Publ., 1990, 36 p.
[6] Kalinin E.K., Dreytser G.A., Yarkho S.A. Intensifikatsiya teploobmena v kanalakh [Heat transfer intensification in pipes]. Moscow, Mashinostroenie Publ., 1990, 208 p.
[7] Ivanov V.L., Leontev A.I., Manushin E.A., Osipov M.I. Teploobmennye apparaty i sistemy okhlazhdeniya gazoturbinnykh i kombinirovannykh ustanovok [Heat exchanger and cooling systems in gas turbine and combined cycle plants]. Moscow, Bauman Moscow State Technical University Publ., 2004, 592 p.
[8] Koch R. Druckverlust und wdrmeubergang bei verwirbelter stromung [Pressure loss and heat transfer for turbulent flow]. VDI-Forschungsheft, 1958, no. 469, s. 144.
[9] Migay V.K. Povyshenie effektivnosti sovremennykh teploobmennikov [Increasing the efficiency of modern heat exchangers]. Moscow, Energia Publ., 1980, 144 p.
[10] Zhukauskas A.A. Teploenergetika - Thermal Engineering, 1984, no. 3, pp. 10-13.