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A system for measuring the heat transfer coefficient of liquid sodium in a thermal entrance regionFletchall, Donald Edward 08 1900 (has links)
No description available.
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An investigation of combined free and forced convection heat transfer in a horizontal, isothermal tubeVillanueva y Guardia, José 08 1900 (has links)
No description available.
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Heat transfer in pulsating flowWells, Roy Allen 08 1900 (has links)
No description available.
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Radiant energy exchange configuration factors for non-Lambertonian surfacesBlanton, Roy Warner 05 1900 (has links)
No description available.
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Overall coefficient of heat transmission of honeycomb structureCapelouto, Isaac 05 1900 (has links)
No description available.
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A study of heat transfer involving a gas with suspended particlesChou, Chia-San 08 1900 (has links)
No description available.
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Entrainment from falling liquid filmsAdams, Jeremy Sorby January 1969 (has links)
Ph.D. thesis 1970 from the Dept. of Chem. Engineering, University of Adelaide / 238 leaves : ill., appendix 152 leaves / Title page, contents and abstract only. The complete thesis in print form is available from the University Library.
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Heat and momentum transfer to a liquid boiling in upwards flow in a vertical annulusDolan, David Sutton January 1969 (has links)
148 leaves : ill., appendix 154 leaves / Title page, contents and abstract only. The complete thesis in print form is available from the University Library. / Thesis (Ph.D.)--University of Adelaide, Dept. of Chemical Engineering, 1972
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The dynamics of packed beds with intraphase heat transferJeffreson, Carl Patrick January 1971 (has links)
1 v. (various pagings) : ill. / Title page, contents and abstract only. The complete thesis in print form is available from the University Library. / Thesis (Ph.D.)--University of Adelaide, Dept. of Chemical Engineering, 1972
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Measurement of heat transfer coefficient in concentric and eccentric annuliChoudhury, Wasiuddin January 1963 (has links)
Heat transfer coefficients were measured at the inner wall of smooth concentric and eccentric annuli. The annuli were formed by an outer plastic tube of 3 in. inside diameter and an inner core cylinder of 1 in outside diameter. Air at room temperature was allowed to flow through the annuli at a Reynolds number range from 15,000 to 65,000.
The measurement of heat transfer coefficient was made by a transient heat transfer test technique. The method consisted in establishing an initial temperature gradient between the fluid and a solid body mounted on the core cylinder by heating, then observing and recording the temperature-time history of the body as it returned to equilibrium condition with the fluid stream. The heat transfer coefficient was calculated from this record.
The final results were presented in graphical form showing variations of Nusselt number with Reynolds number. The results of the concentric annulus tests agreed favourably with those predicted by Wiegand (2) and Monrad and Pelton (3). The effect of eccentricity was to reduce the heat transfer coefficient although the general trend was identical to that in the concentric annulus case.
It was observed that the decrease of heat transfer coefficient was not linearly related to the eccentricity of the core cylinder. The effect of eccentricity was more pronounced in the range 0 ≤ e ≤ 0.5 where the value of heat transfer coefficient decreased considerably. / Applied Science, Faculty of / Mechanical Engineering, Department of / Graduate
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