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Open AccessJournal ArticleDOI

The effect of pure forced convection on the boiling heat transfer between a two-dimensional subcooled water jet and a heated surface.

Yoshiki Miyasaka, +1 more
- 20 Feb 1980 - 
- Vol. 13, Iss: 1, pp 22-28
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TLDR
In this paper, the effect of pure forced convection on heat transfer with boiling in a flow of subcooled water was investigated in two flow fields of an impinging water jet, at the stagnation point and in the parallel flow zone.
Abstract
This paper is concerned with heat transfer from a heated surface with uniform heat flux to a two-dimensional water jet. It describes quantitatively the results on the effect of pure forced convection on heat transfer with boiling in a flow of subcooled water. Experiments were carried out in two flow fields of an impinging water jet, at the stagnation point and in the parallel flow zone. Approximation of the superposition, that is, the total heat flux at forced convective boiling consisting of pool boiling heat flux and pure convective heat flux, held fairly good up to the burn-out heat flux region.

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Single-Phase Liquid Jet Impingement Heat Transfer

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Jet Impingement Boiling

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TL;DR: In this article, the authors focus on the fundamental issues that influence boiling heat transfer to a free-surface, planar jet of water and present local boiling curves at several streamwise distances from the stagnation line, while streamwise distributions of the surface temperature and convection coefficient.
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Controlled cooling of a hot plate with a water jet

TL;DR: In this article, an inverse heat conduction problem is used to calculate the local heat flux and corresponding temperature up to a distance of 55 mm from the stagnation line of a planar jet of water.
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Local convective heat transfer from a heated surface to an impinging, planar jet of water

TL;DR: In this article, surface temperature and heat flux distributions have been measured on a flat, upward facing, constant heat flux surface cooled by a planar, impinging water jet, and the results for the stagnation and boundary layer flows are correlated by expressions of the form Nu = CRenPrm.
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