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Heat Transfer Research

Publicado 18 números por año

ISSN Imprimir: 1064-2285

ISSN En Línea: 2162-6561

The Impact Factor measures the average number of citations received in a particular year by papers published in the journal during the two preceding years. 2017 Journal Citation Reports (Clarivate Analytics, 2018) IF: 1.7 To calculate the five year Impact Factor, citations are counted in 2017 to the previous five years and divided by the source items published in the previous five years. 2017 Journal Citation Reports (Clarivate Analytics, 2018) 5-Year IF: 1.4 The Immediacy Index is the average number of times an article is cited in the year it is published. The journal Immediacy Index indicates how quickly articles in a journal are cited. Immediacy Index: 0.6 The Eigenfactor score, developed by Jevin West and Carl Bergstrom at the University of Washington, is a rating of the total importance of a scientific journal. Journals are rated according to the number of incoming citations, with citations from highly ranked journals weighted to make a larger contribution to the eigenfactor than those from poorly ranked journals. Eigenfactor: 0.00072 The Journal Citation Indicator (JCI) is a single measurement of the field-normalized citation impact of journals in the Web of Science Core Collection across disciplines. The key words here are that the metric is normalized and cross-disciplinary. JCI: 0.43 SJR: 0.318 SNIP: 0.568 CiteScore™:: 3.5 H-Index: 28

Indexed in

A BUBBLE-LAYER-BASED MECHANISTIC MODEL FOR THE SATURATED FLOW BOILING IN VERTICAL CHANNELS

Volumen 54, Edición 4, 2023, pp. 25-46
DOI: 10.1615/HeatTransRes.2022044816
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SINOPSIS

Saturated flow boiling contains complex bubble behaviors and interactions such as sliding, lift-off and coalescence. Currently, the prediction of this process mainly depends on numerical simulations combined with bubble-behavior-related submodels, or a combination of one-dimensional empirical correlations without considering bubble dynamics. Meanwhile, the theoretical analysis is still lacking. Therefore, this paper focuses on the development of a mechanistic model for this process which divides the flow field into different regions in the radial direction due to different bubble motions. Then, mass, energy and momentum exchanges between different regions are considered and reflected through a new set of two-dimensional steady-state conservation equations combined with a modified slip ratio correlation. The present model is verified with experimental data of cross-sectional void fraction profiles in vertical channels which shows pretty high accuracy. On this basis, mass flux between different regions in the radial direction, and distributions of several parameters, such as the vapor quality, velocity and mass flow rates in each region along the channel direction are obtained and analyzed. In comparison, the present model can reveal more detailed information than one-dimensional correlations and can provide a simple, fast and stable way to predict the saturated flow boiling process.

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