The efficiency of heat transfer in heat exchangers having a staggered and in-line arrangement of a tube bundle is compared. The dependence of pressure losses on the minimum relative tube pitch for the considered arrangements of tubes at various Reynolds numbers is shown. Using heat exchangers with staggered tube arrangements at production facilities for chemical fibers is substantiated.
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Translated from Khimicheskie volokna, No.6, pp. 62–64, 2021
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Tyurin, M.P., Borodina, E.S., Aparushkina, M.A. et al. Performance Analysis of Shell-and-Tube Heat Exchanger. Fibre Chem 53, 431–433 (2022). https://doi.org/10.1007/s10692-022-10322-5
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DOI: https://doi.org/10.1007/s10692-022-10322-5