2001
DOI: 10.1016/s0960-1481(00)00149-x
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Theoretical analysis of laminar-film condensation heat transfer inside inclined wickless heat pipes flat-plate solar collector

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Cited by 51 publications
(19 citation statements)
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“…Heat pipes eliminate the welding and scale formation while it gives 88% efficiency with low cost. [38] suggest that the pipe inclination angle have a substantial effect on heat transfer inside the wickless heat pipe. Similarly [39] shows that the increase in number of wickless heat pipe gives a significant effect on the collector efficiency.…”
Section: Micro Tubes Flat Plate Collectormentioning
confidence: 98%
“…Heat pipes eliminate the welding and scale formation while it gives 88% efficiency with low cost. [38] suggest that the pipe inclination angle have a substantial effect on heat transfer inside the wickless heat pipe. Similarly [39] shows that the increase in number of wickless heat pipe gives a significant effect on the collector efficiency.…”
Section: Micro Tubes Flat Plate Collectormentioning
confidence: 98%
“…The solution can also be used for condensation inside tubes. Hussein et al (2001) proposed a numerical model, also derived from Nusselt's theory, but for an application of condensation in thermosyphons. In the model, a steady-state two-dimensional model is solved to determine the liquid film thickness.…”
Section: Thermal Modelling Of Separated Condensing Flowsmentioning
confidence: 99%
“…In the model, a steady-state two-dimensional model is solved to determine the liquid film thickness. Both in the Fieg and Roetzel (1994) and in the Hussein et al (2001) models, gravitational and shear forces are taken into account but capillary forces are neglected. A major assumption of these models is that the liquid film thickness is supposed to be small compared with the tube radius.…”
Section: Thermal Modelling Of Separated Condensing Flowsmentioning
confidence: 99%
“…For small thermosyphon length to radii ratios (L c /r i ≤ 20), the thermosyphon tube is modeled as laminar film condensation on a flat inclined surface, where the condensed film returns to the evaporator by gravity and evaporates completely by the end of the evaporator section (i.e., no liquid pool exists at the base of the 7 evaporator). However, for larger length to radii ratios (L c /r i > 20), a modified heat transfer coefficient correlation is used that better captures the circumferential liquid film thickness variation due to thermosyphon inclination (Hussein, 2001). The vapor is assumed to be at saturation conditions, and shear forces are negligible (Faghri, 1995) resulting in thermal resistances of evaporation and condensation heat transfer described by Eqns.…”
Section: Thermosyphon Modelingmentioning
confidence: 99%