Boiling and Evaporation in Small Diameter Channels

Bergles, A. E.; Lienhard, John H.; Kendall, Gail E.; Griffith, P.

doi:10.1080/01457630304041

Cited by 171 publications

(67 citation statements)

References 49 publications

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“…A part of the data shows accordance of heat transfer process to developed boiling and another part demonstrates qualitatively differing trends [104][105][106][107][108].…”

Section: Duration-dependent Multifactoring and Boiling In Microsystemsmentioning

confidence: 99%

Boiling Heat Transfer: Mechanisms, Models, Correlations and the Lines of Further Research

Shekriladze¹

2008

TOMEJ

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A review discusses current status of boiling heat transfer research. Basic experimental facts, physical models and correlations of experimental data on heat transfer coefficient (HTC) are reconsidered. Principal restrictions of traditional model of "the theatre of actors" (MTA) are demonstrated. Basic role of control of HTC by thermodynamic conditions on nucleation sites is demonstrated and consequent model of "the theatre of director" (MTD) is discussed. Universal MTD-based correlation of boiling HTC of all types of liquids is presented. Unified consistent research framework for developed boiling heat transfer and diverse specific boiling heat transfer regimes is outlined through supplementing MTD by so-called multifactoring concept (MFC). MFC links transition from developed boiling mode to diverse boiling curves to a phenomenon of multiplication of factors influencing HTC. Multifactoring phenomenon equally can cover any boiling process including boiling in minichannels and microchannels. Possible types of multifactoring are considered. Finally, the ways of further research of the boiling problem are discussed.

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“…A part of the data shows accordance of heat transfer process to developed boiling and another part demonstrates qualitatively differing trends [104][105][106][107][108].…”

Section: Duration-dependent Multifactoring and Boiling In Microsystemsmentioning

confidence: 99%

Boiling Heat Transfer: Mechanisms, Models, Correlations and the Lines of Further Research

Shekriladze¹

2008

TOMEJ

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“…The boiling mechanism was found to be determined by the wall surface conditions rather than the channel dimensions. Bergles et al [17] also performed an analysis and showed that incipience of boiling in a subcooled flow was most likely governed by the nucleation sites in the walls and not by the channel size. Saitoh et al [18] experimentally investigated the boiling heat transfer of refrigerant R-134a flow in three horizontal tubes of diameter 0.51, 1.12, and 3.1 mm and mass fluxes ranging from 150 to 450 kg/m 2 s. Their study showed that the local heat transfer coefficient increased with increasing mass flux in larger tubes but was not significantly affected by mass flux in smaller tubes.…”

Section: Introductionmentioning

confidence: 99%

Microchannel size effects on local flow boiling heat transfer to a dielectric fluid

Harirchian

Garimella

2008

International Journal of Heat and Mass Transfer

249

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“…Two-phase microchannel heat sinks are attractive to cool advanced electronic devices because they harness the latent heat of vaporization to dissipate high heat fluxes in a compact form factor. However, minimizing flow instabilities during boiling while enhancing the critical heat flux (CHF) to maximize heat dissipation has been difficult to achieve [4][5][6]. These flow instabilities which can be triggered by several mechanisms including explosive bubble expansion [7], upstream compressibility [8,9] and density wave oscillation [10] can lead to large pressure drop fluctuations across the channels and temperature spikes associated with liquid dry-out.…”

Section: Introductionmentioning

confidence: 99%