Heat Transfer During Subcooled Boiling in Tubes (A Review)

This article provides a review of the correlations and models for determining the intensity of heat transfer during subcooled boiling in pipes. As a rule, correlations are based on dimensionless similarity numbers, while heat exchange models with subcooled boiling use the principle of superposition...

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Main Authors: Pavlo G. Gakal, Gennadiy A. Gorbenko, Rustem Yu. Turna, Edem R. Reshitov
Format: Article
Language:English
Published: NAS of Ukraine, A. Pidhornyi Institute of Mechanical Engineering Problems 2019-03-01
Series:Journal of Mechanical Engineering
Subjects:
Online Access:https://journal-me.com/archive/en/2019/2019_1_2_eng.pdf
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author Pavlo G. Gakal
Gennadiy A. Gorbenko
Rustem Yu. Turna
Edem R. Reshitov
author_facet Pavlo G. Gakal
Gennadiy A. Gorbenko
Rustem Yu. Turna
Edem R. Reshitov
author_sort Pavlo G. Gakal
collection DOAJ
description This article provides a review of the correlations and models for determining the intensity of heat transfer during subcooled boiling in pipes. As a rule, correlations are based on dimensionless similarity numbers, while heat exchange models with subcooled boiling use the principle of superposition of the components of heat transfer during forced convection and developed nucleate boiling. Various authors propose different approaches to the implementation of the principle of superposition. This article presents an analysis of the advantages and disadvantages of the correlations and models. These advantages and disadvantages were determined both by analyzing the physical laws of subcooled boiling and by comparing the results that were obtained by the authors of this article by means of various models of subcooled boiling with the experimental data obtained during the study of heat transfer during the subcooled boiling of ammonia in a cylindrical heated tube. The tube diameter d was 6.9 mm, length L was 150 mm, inlet subcooling was 5 K, saturation temperature range was 61...65 °C, mass flow rate was 7.5 g/s, and heat flux density range was 5...18 W/cm2. As a result of the review and comparison with the experimental data, it was determined that the existing correlations and models describe the subcooled boiling of ammonia with insufficient accuracy, especially in the area of the combined effect of forced convection and nucleate boiling. Therefore, it is necessary either to refine the existing correlations and models, or develop new models for a more precise description of the subcooled boiling heat transfer of ammonia in heated tubes in the parameter range specified above.
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spelling doaj.art-e84646a6535c44fa9a3ca7710ed20de92022-12-21T22:45:23ZengNAS of Ukraine, A. Pidhornyi Institute of Mechanical Engineering ProblemsJournal of Mechanical Engineering2709-29842709-29922019-03-0122191610.15407/pmach2019.01.009Heat Transfer During Subcooled Boiling in Tubes (A Review)Pavlo G. Gakal0https://orcid.org/0000-0003-3043-2448Gennadiy A. Gorbenko1Rustem Yu. Turna2Edem R. Reshitov3National Aerospace University KhAINational Aerospace University KhAINational Aerospace University KhAINational Aerospace University KhAIThis article provides a review of the correlations and models for determining the intensity of heat transfer during subcooled boiling in pipes. As a rule, correlations are based on dimensionless similarity numbers, while heat exchange models with subcooled boiling use the principle of superposition of the components of heat transfer during forced convection and developed nucleate boiling. Various authors propose different approaches to the implementation of the principle of superposition. This article presents an analysis of the advantages and disadvantages of the correlations and models. These advantages and disadvantages were determined both by analyzing the physical laws of subcooled boiling and by comparing the results that were obtained by the authors of this article by means of various models of subcooled boiling with the experimental data obtained during the study of heat transfer during the subcooled boiling of ammonia in a cylindrical heated tube. The tube diameter d was 6.9 mm, length L was 150 mm, inlet subcooling was 5 K, saturation temperature range was 61...65 °C, mass flow rate was 7.5 g/s, and heat flux density range was 5...18 W/cm2. As a result of the review and comparison with the experimental data, it was determined that the existing correlations and models describe the subcooled boiling of ammonia with insufficient accuracy, especially in the area of the combined effect of forced convection and nucleate boiling. Therefore, it is necessary either to refine the existing correlations and models, or develop new models for a more precise description of the subcooled boiling heat transfer of ammonia in heated tubes in the parameter range specified above.https://journal-me.com/archive/en/2019/2019_1_2_eng.pdfsubcooled boilingnucleate boilingforced convectionmodels of subcooled boilingprinciple of superpositionammonia
spellingShingle Pavlo G. Gakal
Gennadiy A. Gorbenko
Rustem Yu. Turna
Edem R. Reshitov
Heat Transfer During Subcooled Boiling in Tubes (A Review)
Journal of Mechanical Engineering
subcooled boiling
nucleate boiling
forced convection
models of subcooled boiling
principle of superposition
ammonia
title Heat Transfer During Subcooled Boiling in Tubes (A Review)
title_full Heat Transfer During Subcooled Boiling in Tubes (A Review)
title_fullStr Heat Transfer During Subcooled Boiling in Tubes (A Review)
title_full_unstemmed Heat Transfer During Subcooled Boiling in Tubes (A Review)
title_short Heat Transfer During Subcooled Boiling in Tubes (A Review)
title_sort heat transfer during subcooled boiling in tubes a review
topic subcooled boiling
nucleate boiling
forced convection
models of subcooled boiling
principle of superposition
ammonia
url https://journal-me.com/archive/en/2019/2019_1_2_eng.pdf
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AT gennadiyagorbenko heattransferduringsubcooledboilingintubesareview
AT rustemyuturna heattransferduringsubcooledboilingintubesareview
AT edemrreshitov heattransferduringsubcooledboilingintubesareview