Natural Convection Film Boiling Heat Transfer

Clements, L. D.; Colver, C. Phillip

doi:10.1021/ie50729a006

Cited by 17 publications

(4 citation statements)

References 62 publications

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“…Eqs. (4) and (5). For each flow regime the pcoposed correlation again followed two distinct trends, one for the We /a.…”

Section: Predictive Equations For the Axial Extent Of Flow Regimesmentioning

confidence: 74%

“…From a detailed study of an adiabatic, single'phase (liquid) jet core inverted annular flow [30], it was established conclusively that the correlated jet core break-up data followed two distinct trends; one for the region over which the jet break-up length was independent of the inlet annulus void fraction (a^), the annulus gas-liquid jet inlet relative velocity, and the gas density, with a marked sensitivity of the break-up to these variables for the second region. The break-up lengths for these two regions were closely approximated by the following equations: = 480 Re" 0 ' 53 We 0 ' 5 (4) D J J J -0.645 (5) Since these two curves intersect at We /a. = 1.73, this critical value of gas Weber number over the square of the T.hlet annulus void fraction provides a useful criterion for determining the validity range for each equation.…”

Section: Predictive Equations For the Axial Extent Of Flow Regimesmentioning

confidence: 99%

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Two-phase flow characteristic of inverted bubbly, slug and annular flow in post-critical heat flux region

Ishii

Denten

1990

Nuclear Engineering and Design

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Inverted annular flow can be visualized as a liquid jet-like core surrounded by a vapor annulus. While many analytical and experimental studies of heat transfer in this regime have been performed, there is very little understanding of the basic hydrodynamics of the post-CHF flow field. However, a recent experimental study was done that was able to successfully investigate the effects of various steady-state inlet flow parameters on the post-CHF hydrodynamics of the film boiling of a single phase liquid jet. This study was carried out by means of a visual photographic analysis of an idealized single phase core inverted annular flow initial geometry (single phase liquid jet core surrounded by a coaxial annulus of gas). In order to extend this study, a subsequent flow visualization of an idealized two-phase core inverted annular flow geometry (two-phase central jet core, surrounded by a coaxial annulus of gas) was carried out. The objective of this second experimental study was to investigate the effect of steadystate inlet, pre-CHF two-phase jet core parameters on the hydrodynamics of the post-CHF flow field. In actual film boiling situations, two-phase flows with net positive qualities at the CHF point are encountered. Thus, the focus of the present experimental study was on the inverted bubbly, slug, and annular flow fields in the post dryout film boiling region. Observed post dryout hydrodynamic behavior is reported. A correlation for the axial extent of the transition flow pattern between inverted annular and dispersed droplet flow (the agitated regime) is developed. It is shown to depend strongly on inlet jet core parameters and jet void fraction at the dryout point. DISCLAIMER This report was prepared as an account of work sponsored by an agency of the United States Government. Neither the United States Government nor any agency thereof, nor any of their employees, makes any warranty, express or implied, or assumes any legal liability or responsibility for the accuracy, completeness, or usefulness of any information, apparatus, product, or process disclosed, or represents that its use would not infringe privately owned rights. Reference herein to any specific commercial product, process, or service by trade name, trademark, manufacturer, or othrrwise does not necessarily constitute or imply its endorsement, recommendation, or favoring by the United Stales Government or any agency thereof. The views and opinions of authors expressed herein do not necessarily state or reflect those of the United States Government or any agency thereof.

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“…Eqs. (4) and (5). For each flow regime the pcoposed correlation again followed two distinct trends, one for the We /a.…”

Section: Predictive Equations For the Axial Extent Of Flow Regimesmentioning

confidence: 74%

Section: Predictive Equations For the Axial Extent Of Flow Regimesmentioning

confidence: 99%

Two-phase flow characteristic of inverted bubbly, slug and annular flow in post-critical heat flux region

Ishii

Denten

1990

Nuclear Engineering and Design

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show abstract

“…Operational domain in the stability plane is bounded by the physical restriction on heat flux and subcooling. For positive subcooling, if Ais denotes the maximum possible subcooling, then (19) and (20) represent the basic characteristics in the stability plane. Figure (2) shows the stability plane with these basic characteristics.…”

Section: Stability Plane"mentioning

confidence: 99%

“…Most of the research on the post-CHF region dealt mainly with heat transfer. Excellent reviews of the widespread literature were provided by Jordan [19] and Clemments and Clover [20]. A subsequent review by Kalinin et alJ21] considered both free and forced convective film boiling in great detail.…”

Section: State Of the Arts Reviewmentioning

confidence: 99%