Forced convection boiling sodium studies at low pressure
Two-phase flow of forced convection boiling sodium at high temperatures
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Two-phase flow of forced convection boiling sodium at high temperatures
Density wave, pressure drop and thermal flow oscillation modes in forced-convection boiling Freon 11
Apparatus for temperature and pressure drop measurements of forced convection condensing potassium heat transfer
Pressure drop oscillations in forced convection flow of Freon-11 near onset of boiling, noting flow rate for instability and limit cycles
Forced convection heat transfer from flat plate and cylinder in cross flow to simulated Mars atmosphere
Determination of boundary layer diffusion in forced convection flow
Vaporization caused by incipient boiling in forced convective flow of superheated liquid
Measuring apparatus and techniques for heat transfer and pressure drop data in forced convection boiling potassium
Forced convective heat transfer to a fluid between two parallel plates having a wall heat flux as a function of axial position and time
Forced convection heat transfer correlations for hydrogen, helium, and nitrogen gases flowing through helical tungsten wire matrices at high surface temperatures
Heat transfer and pressure drop measurements for high temperature boiling potassium in forced convection
A simple engineering correlation scheme is developed to predict the variable property effects on dilute species laminar forced convection mass transfer applicable to all vapor molecules or Brownian diffusing small particle, covering the surface to mainstream temperature ratio of 0.25 T sub W/T sub e 4. The accuracy of the correlation is checked against rigorous numerical forced convection laminar boundary layer calculations of flat plate and stagnation point flows of air containing trace species of Na, NaCl, NaOH, Na2SO4, K, KCl, KOH, or K2SO4 vapor species or their clusters. For the cases reported here the correlation had an average absolute error of only 1 percent (maximum 13 percent) as compared to an average absolute error of 18 percent (maximum 54 percent) one would have made by using the constant-property results.
Stability of Freon-11 and water flow oscillations in forced convection boiling
Forced-convection boiling at low heat flux and flow velocities in zero gravity for slightly subcooled distilled water
The inception of bubbles during forced convection was studied experimentally by using trichlorotrifluoroethane (R-113 or Freon-113). The experiments were performed in a rectangular channel, 12.7 x 9.5 mm in cross section. Heating was from a 3.2 mm wide strip embedded in the longer side of the channel. The pressures studied ranged from 3.6 to 20.7 bar, mass velocities from 700 to 600 kg/sq m/sec, and inlet subcoolings from 26 to 97 C. Photographs of the flow were used to determine when bubbles first appeared on the heated surface. These data were compared with wall temperature measurements and inception theories. A reasonable method for calculating the complete boiling curve was found to agree with these results.
Wall temperature distribution for laminar forced convection in rectangular channels with unequal heat addition on adjacent sides
Heat transfer and fluid flow during forced convection vaporization of high temperature potassium
A temperature gradient stage design for optical microscopy is described. Exceptional thermal stability is the major feature. The stage is used to study crystal growth phenomena occurring at the solid-liquid interface. The apparatus is designed to use transparent organic solutions as models for the study of metal-like solidification. The stage provides a controlled thermal environment for unidirectional solidification of low melting temperature materials. Freezing rate is regulated by mechanically sliding in the stage a thin glass cell containing the materials being studied. Two cell assemblies are described. One type is used for convection-free and the other for controlled forced convection studies of the solidification interface.