Study of Turbulent Single-phase Heat Transfer and Onset of Nucleate Boiling in High Aspect Ratio Mini-channels to Support the MITR LEU Conversion

Study of Turbulent Single-phase Heat Transfer and Onset of Nucleate Boiling in High Aspect Ratio Mini-channels to Support the MITR LEU Conversion PDF Author: Eric Christopher Forrest
Publisher:
ISBN:
Category :
Languages : en
Pages : 425

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Book Description
Heat transfer in high aspect ratio mini-channels has important applications for materials test reactors using plate-type fuel. These fuel plates typically possess coolant channels with hydraulic diameters on the order of 4 mm or less. The single and two-phase heat transfer in such channels has not been well-characterized, especially in regard to the onset of nucleate boiling. While surface effects are known to dramatically influence the incipience of boiling, they have not been widely considered under forced convection. Since the limiting safety system setting for the MITR is the onset of nucleate boiling, there is considerable interest in better characterizing the phenomenon in such channels. This study presents a first-of-a-kind, two-phase flow facility designed to measure the single-phase heat transfer coefficient and onset of nucleate boiling in a high aspect ratio mini-channel over a wide range of flow conditions while also permitting high speed visualization of the entire surface. The single-phase heat transfer coefficient is measured for mass fluxes ranging from 750 kg/m2-sec up to 6000 kg/m2 -sec and for sub-coolings ranging from 20 °C to 70 °C. The onset of nucleate boiling superheat and heat flux are measured for mass fluxes ranging from 750 kg/m2- sec to 3000 kg/m2-sec and for sub-coolings ranging from 10 °C to 45 °C. Measurements are supported with high speed videography to visualize bubble incipience when conditions permit. The influence of surface wettability on the incipience point is also investigated by performing tests on a surface oxidized at high temperature in air. Using a boundary layer analysis along with experimental data obtained in the study, a semi-analytical correlation is developed to predict the single-phase heat transfer coefficient in high aspect ratio rectangular channels. The correlation accounts for effects from secondary flows and heating asymmetry, and is suitable for both the transition and fully turbulent flow regimes. The new correlation predicts the Nusselt number with a mean absolute error of 4.9% in the range of 2.2

Study of Turbulent Single-phase Heat Transfer and Onset of Nucleate Boiling in High Aspect Ratio Mini-channels to Support the MITR LEU Conversion

Study of Turbulent Single-phase Heat Transfer and Onset of Nucleate Boiling in High Aspect Ratio Mini-channels to Support the MITR LEU Conversion PDF Author: Eric Christopher Forrest
Publisher:
ISBN:
Category :
Languages : en
Pages : 425

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Book Description
Heat transfer in high aspect ratio mini-channels has important applications for materials test reactors using plate-type fuel. These fuel plates typically possess coolant channels with hydraulic diameters on the order of 4 mm or less. The single and two-phase heat transfer in such channels has not been well-characterized, especially in regard to the onset of nucleate boiling. While surface effects are known to dramatically influence the incipience of boiling, they have not been widely considered under forced convection. Since the limiting safety system setting for the MITR is the onset of nucleate boiling, there is considerable interest in better characterizing the phenomenon in such channels. This study presents a first-of-a-kind, two-phase flow facility designed to measure the single-phase heat transfer coefficient and onset of nucleate boiling in a high aspect ratio mini-channel over a wide range of flow conditions while also permitting high speed visualization of the entire surface. The single-phase heat transfer coefficient is measured for mass fluxes ranging from 750 kg/m2-sec up to 6000 kg/m2 -sec and for sub-coolings ranging from 20 °C to 70 °C. The onset of nucleate boiling superheat and heat flux are measured for mass fluxes ranging from 750 kg/m2- sec to 3000 kg/m2-sec and for sub-coolings ranging from 10 °C to 45 °C. Measurements are supported with high speed videography to visualize bubble incipience when conditions permit. The influence of surface wettability on the incipience point is also investigated by performing tests on a surface oxidized at high temperature in air. Using a boundary layer analysis along with experimental data obtained in the study, a semi-analytical correlation is developed to predict the single-phase heat transfer coefficient in high aspect ratio rectangular channels. The correlation accounts for effects from secondary flows and heating asymmetry, and is suitable for both the transition and fully turbulent flow regimes. The new correlation predicts the Nusselt number with a mean absolute error of 4.9% in the range of 2.2

Survey of the Literature Pertaining to the Phenomena of Nucleate Boiling

Survey of the Literature Pertaining to the Phenomena of Nucleate Boiling PDF Author: R. A. Rockow
Publisher:
ISBN:
Category : Fouling
Languages : en
Pages : 58

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Nya frimärksklubbens och Skånska social-demokratens utställning "Min hobby" i Jacob Hansens hus, Hälsingborg 16 -18 maj 1953

Nya frimärksklubbens och Skånska social-demokratens utställning Author:
Publisher:
ISBN:
Category :
Languages : en
Pages : 15

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A Review and Assessment of Boiling Heat Transfer and the Departure from Nucleate Boiling

A Review and Assessment of Boiling Heat Transfer and the Departure from Nucleate Boiling PDF Author: Gerhard O. Mueller
Publisher:
ISBN:
Category : Nucleate boiling
Languages : en
Pages : 196

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Nucleate-boiling Studies with Aqueous ThO2 Slurries

Nucleate-boiling Studies with Aqueous ThO2 Slurries PDF Author: D. G. Thomas
Publisher:
ISBN:
Category : Nuclear reactions
Languages : en
Pages : 32

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Ìtan Ìnú Ìwé Mimó. [With illustrations.].

Ìtan Ìnú Ìwé Mimó. [With illustrations.]. PDF Author:
Publisher:
ISBN:
Category :
Languages : en
Pages :

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A Dimensional Analysis of the Departure from Nucleate Boiling Heat Flux in Forced Convection

A Dimensional Analysis of the Departure from Nucleate Boiling Heat Flux in Forced Convection PDF Author: Peter Griffith
Publisher:
ISBN:
Category : Heat
Languages : en
Pages : 38

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Flow Boiling in Expanding Microchannels

Flow Boiling in Expanding Microchannels PDF Author: Tamanna Alam
Publisher: Springer
ISBN: 3319550322
Category : Science
Languages : en
Pages : 89

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Book Description
This Brief presents an up to date summary of details of the flow boiling heat transfer, pressure drop and instability characteristics; two phase flow patterns of expanding microchannels. Results obtained from the different expanding microscale geometries are presented for comparison and addition to that, comparison with literatures is also performed. Finally, parametric studies are performed and presented in the brief. The findings from this study could help in understanding the complex microscale flow boiling behavior and aid in the design and implementation of reliable compact heat sinks for practical applications.

A Correlation for Nucleate Flow Boiling in Small Channels

A Correlation for Nucleate Flow Boiling in Small Channels PDF Author:
Publisher:
ISBN:
Category :
Languages : en
Pages : 30

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Book Description
Compact heat exchangers are becoming more attractive for applications in which energy conservation, space saving, and cost are important considerations. Applications exist in the process industries where phase-change heat transfer realizes more compact designs and improved performance compared to single-phase heat transfer. However, there have been only a few studies in the literature reporting on phase-change heat transfer and two-phase flow in compact heat exchangers, and validated design correlations are lacking. Recent data from experiments on flow boiling of refrigerants in small channels have led researchers to conclude that nucleation is the dominant heat transfer mechanism over a broad range of heat flux and wall superheats. Local heat transfer coefficients and overall two-phase pressure drops were measured for three different refrigerants with circular and non-circular channels in a range of pressures. This data base supports the nucleate boiling mechanism, and it was used to develop a new correlation for heat transfer in nucleate flow boiling. The correlation is based on the Rohsenow boiling model, introducing a confinement number defined by Kew and Cornwell. The new correlation predicts the experimental data for nucleate flow boiling of three refrigerants within "15%.

Critical Heat Flux in Flow Boiling in Microchannels

Critical Heat Flux in Flow Boiling in Microchannels PDF Author: Sujoy Kumar Saha
Publisher: Springer
ISBN: 3319177354
Category : Science
Languages : en
Pages : 62

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Book Description
This Brief concerns the important problem of critical heat flux in flow boiling in microchannels. A companion edition in the SpringerBrief Subseries on Thermal Engineering and Applied Science to “Heat Transfer and Pressure Drop in Flow Boiling in Microchannels,” by the same author team, this volume is idea for professionals, researchers, and graduate students concerned with electronic cooling.