Open AccessDissertation
Heat transfer and pressure drop for evaporation of water in a vertical tube
TLDR
Thesis (Sc. D. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1953 as discussed by the authors, Boston, Massachusetts, United States, USA, USAAbstract:
Thesis (Sc. D.)--Massachusetts Institute of Technology, Dept. of Chemical Engineering, 1953.read more
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Journal ArticleDOI
A general correlation for flow boiling in tubes and annuli
K.E. Gungor,R.H.S. Winterton +1 more
TL;DR: In this article, a new general correlation for forced convection boiling has been developed with the aid of a large data bank consisting of over 4300 data points for water, refrigerants and ethylene glycol, covering seven fluids and 28 authors.
Journal ArticleDOI
Flow Boiling Heat Transfer in Vertical Tubes Correlated by an Asymptotic Model
Dieter Steiner,Jerry Taborek +1 more
TL;DR: In this article, a new model, based on asymptotic addition of the two boiling components, is introduced It follows the established principles of flow boiling and converges correctly to the extremes of all parameters Tested on the University of Karlsruhe data bank containing over 13,000 data points in vertical flow boiling, results superior to previous correlations are demonstrated
Journal ArticleDOI
Forced convection boiling in tubes
TL;DR: In this article, local heat transfer coefficients and pressure gradients have been measured for bulk boiling of water in forced flow (vertically upward) in round tubes with internal diameters ranging from 1162 to
ReportDOI
Contribution to the theory of two-phase, one-component critical flow
TL;DR: In this paper, the authors proposed a two-phase flow model based on the one-dimensional model proposed by Lockhar and Martinelli (1902) and showed that it is possible to estimate the rate of change in the axial component of momentum.
Journal ArticleDOI
Correlation of forced convection boiling heat transfer data
TL;DR: In this article, the method of superposition for correlating forced convection boiling heat transfer data is extended to cover subcooled to high quality ranges using single phase and two phase forcing convection equations, a pool boiling equation, and an incipient boiling criterion.