Laminar forced convection in rectangular channels with unequal heat addition on adjacent sides.
Wall temperature distribution for laminar forced convection in rectangular channels with unequal heat addition on adjacent sides
Engineering topics
Publications and source records attributed to Siegel, R..
Wall temperature distribution for laminar forced convection in rectangular channels with unequal heat addition on adjacent sides
Nucleate boiling bubble dynamics in saturated distilled water for various reduced gravity fields
Effects of radiation and convective heat transfer on the wall temperature distributions in an asymmetrically-heated parallel plate channel with gas flowing through it
Forced convective heat transfer to a fluid between two parallel plates having a wall heat flux as a function of axial position and time
Heat transfer by combined forced convection and thermal radiation in a heated tube
Laminar heat transfer in a channel with unsteady flow and wall heating varying with position and time
Analysis of laminar fully developed heat transfer in thin rectangular channels with fuel loading removed from the corners
Convective and radiant heat transfer for flow of a transparent gas in a tube with a gray wall
A pool boiling apparatus was mounted on a counterweighted platform which could be dropped a distance of nine feet. By varying the size of the counterweight, the effective gravity field on the equipment was adjusted between zero and unity. A study of boiling burnout in water indicated that a variation in the critical heat flux according to the one quarter power of gravity was reasonable. A consideration of the transient burnout process was necessary in order to properly interpret the data. A photographic study of nucleate boiling showed how the velocity of freely rising vapor bubbles decreased as gravity was reduced. The bubble diameters at the time of breakoff from the heated surface were found to vary inversely as gravity to the 1/3.5 power. Motion pictures were taken to illustrate both nucleate and film boiling in the low gravity range.
Explore the source record for details and available documents.
The purpose of this note is to examine in a more precise way how the Nusselt numbers for turbulent heat transfer in both the fully developed and thermal entrance regions of a circular tube are affected by two different wall boundary conditions. The comparisons are made for: (a) Uniform wall temperature (UWT); and (b) uniform wall heat flux (UHF). Several papers which have been concerned with the turbulent thermal entrance region problem are given. 1 Although these analyses have all utilized an eigenvalue formulation for the thermal entrance region there were differences in the choices of eddy diffusivity expressions, velocity distributions, and methods for carrying out the numerical solutions. These differences were also found in the fully developed analyses. Hence when making a comparison of the analytical results for uniform wall temperature and uniform wall heat flux, it was not known if differences in the Nusselt numbers could be wholly attributed to the difference in wall boundary conditions, since all the analytical results were not obtained in a consistent way. To have results which could be directly compared, computations were carried out for the uniform wall temperature case, using the same eddy diffusivity, velocity distribution, and digital computer program employed for uniform wall heat flux. In addition, the previous work was extended to a lower Reynolds number range so that comparisons could be made over a wide range of both Reynolds and Prandtl numbers.