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Prediction of flow boiling heat transfer coefficient for carbon dioxide in minichannels and conventional channels

Abstract

In the paper presented are the results of calculations using authors own model to predict heat transfer coefficient during flow boiling of carbon dioxide. The experimental data from various resea rches were collected. Calculations were conducted for a full range of quality variation and a wide range of mass velocity. The aim of the study was to test the sensitivity of the in-house model. The results show the importance of taking into account the surface tension as the parameter exhibiting its importance in case of the flow in minichannels as well as the influence of reduced pressure. The calculations were accomplished to test the sensitivity of the heat transfer model with respect to selection of the appropriate two-phase flow multiplier, which is one of the elements of the heat transfer model. For that purpose correlations due to Müller Steinhagen and Heck as well as the one due to Friedel were considered. Obtained results show a good consistency with experimental results, however the selection of two-phase flow multiplier does not significantly influence the consistency of calculations.

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Accepted or Published Version
DOI:
Digital Object Identifier (open in new tab) 10.1515/aoter-2016-0014
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Creative Commons: CC-BY-NC-ND open in new tab

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Details

Category:
Articles
Type:
artykuły w czasopismach recenzowanych i innych wydawnictwach ciągłych
Published in:
Archives of Thermodynamics no. 37, pages 89 - 106,
ISSN: 1231-0956
Language:
English
Publication year:
2016
Bibliographic description:
Mikielewicz D., Jakubowska B.: Prediction of flow boiling heat transfer coefficient for carbon dioxide in minichannels and conventional channels// Archives of Thermodynamics. -Vol. 37., iss. 2 (2016), s.89-106
DOI:
Digital Object Identifier (open in new tab) 10.1515/aoter-2016-0014
Sources of funding:
  • Free publication
Verified by:
Gdańsk University of Technology

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