Direct Measurement of Heat Transfer Rates and Coefficients in Freezing Processes by the Use of Heat Flux Sensors

2003 ◽  
Vol 81 (9) ◽  
pp. 1105-1112 ◽  
Author(s):  
A. Amarante ◽  
J.-L. Lanoisellé ◽  
A. Ramirez
Author(s):  
F. M. ElMahallawy ◽  
E. E. Khalil ◽  
O. Abdel Aal

The present work presents measurements of velocity, temperature and heat transfer rates carried out on a segmented water-cooled cylindrical oil-fired flame tube typical of a 0.56 kg/s packaged fire-tube steam boiler. A prediction procedure, that solves the conservation equations of the various entities, was successfully used to produce computed velocities, temperatures and heat flux distributions. A two-equation turbulence model, a combustion model and a discrete ordinate radiation model were used to approximate the various characteristics of the flow. The combustion model solved the Eulerian equations of the gas phase, and the Lagrangian equations of the droplet motion, heating, evaporation and combustion.


Sensors ◽  
2014 ◽  
Vol 14 (11) ◽  
pp. 21065-21116 ◽  
Author(s):  
Giovanni Carlomagno ◽  
Luigi de Luca ◽  
Gennaro Cardone ◽  
Tommaso Astarita

Author(s):  
A. Richenderfer ◽  
A. Kossolapov ◽  
J. H. Seong ◽  
G. Saccone ◽  
M. Bucci ◽  
...  

The development and validation of mechanistic boiling heat transfer models has been a focal point in the efforts to improve the efficiency and profitability of power generation systems, e.g. nuclear reactors. The primary goal of these models is improving the accuracy of boiling heat transfer simulations and reducing the uncertainty margins that affect both the design and the safety of a system. However, the emergence of these models has also stimulated the need for high-fidelity experiments and experimental data for validation and verification. In this work we present first-of-a-kind data of heat flux partitioning in boiling heat transfer, obtained using cutting-edge diagnostics and post-processing techniques. A HSV camera was used to visualize the boiling surface at 10,000 frames per second with simultaneous front and side views of the two-phase flow. A high-speed IR camera was used to capture the 2-D radiative signal from the boiling surface to visualize bubble nucleation, growth and detachment at a 115 μm/pixel resolution at 2,500 frames per second. A coupled radiation-conduction calibration model was used to calibrate the IR data and extract the full local temperature and heat flux distributions on the boiling surface, which enable a direct measurement of the partitioned heat fluxes. Here we report the results of investigations performed in flow boiling conditions with a mass flux of 500 kg/m2/s, at atmospheric pressure and 10 K of subcooling. These data will be leveraged to inform the development and validation of the next generation of mechanistic boiling heat transfer models, to be used in Computational Fluid Dynamics (CFD) codes for the design and the safety analysis of nuclear reactors.


Author(s):  
Thomas E. Diller ◽  
Chris Williams

Recent research in the development of the “Thermal and Transport Concept Inventory” test (TTCI) has shown that, despite completing several related courses, students have significant misconceptions of heat transfer principles such as the differences between heat, energy and temperature. This lack of conceptual understanding limits students’ problem-solving abilities (and thus their transition to expertise) and their ability to transfer knowledge to other courses and contexts. This research demonstrates how this problem can be addressed by integrating hands-on workshops into a traditional heat transfer lecture course. The workshops are designed to actively engage students in exploration and discovery using authentic problems. Using heat flux sensors allows students to physically observe abstract phenomena that cannot be easily observed.


1983 ◽  
Vol 105 (3) ◽  
pp. 447-453 ◽  
Author(s):  
I. Catton ◽  
W. A. Brinsfield ◽  
S. M. Ghiaasiaan

Melting a miscible substrate by a heated overlying pool of higher density is studied experimentally. The heated pool is either carbon tetrachloride or diiodomethane, and the substrate is frozen benzene. By performing the experiments with heated pools of different densities the effects of pool-to-substrate temperature differences and pool-density to melt-density ratios on melting heat transfer are independently studied. Heat transfer rates are reported as a function of both temperature difference and density ratio. A model is postulated and compared with experimental results. The downward heat flux is found to be essentially independent of temperature differences, while being an increasing function of the density ratio between the pool and the melting solid for large density rations. For low-density ratios a buoyant plume analysis was used to obtain a correlation.


1962 ◽  
Vol 84 (3) ◽  
pp. 251-254 ◽  
Author(s):  
F. K. Deaver ◽  
W. R. Penney ◽  
T. B. Jefferson

An investigation has been made to determine the effect of low frequency oscillations of relatively large amplitude on the rate of heat transfer from a small horizontal wire to water. Frequencies from 0 to 4.25 cps and amplitudes to 2.76 in. were employed. Temperature differences up to 140 deg F provided heat flux from 2000 to 300,000 Btu/hr ft2. A Reynolds number was defined based on the mean velocity of the wire, and it was shown that heat-transfer rates may be predicted by either forced, free, or mixed convection correlations depending on the relative magnitudes of Reynolds and Grashof numbers.


Author(s):  
Mumtaz Hussain Qureshi ◽  
M. Shakaib

Computational Fluid Dynamics (CFD) study is conducted to determine turbulent fluid flow and temperature profiles in rectangular ribbed channels of solar air heater. The results show significant effect of Reynolds number and ribs height and pitch on turbulence and heat transfer rates. When heat flux is defined at the bottom wall, the temperature values increase rapidly near the ribs due to stagnant zones. The heat transfer coefficients are lower at these locations. When heat flux is specified at the top wall, the variation in heat transfer coefficient is relatively smooth. From the research work, the channel containing ribs of 3mm and pitch 40mm are determined suitable due to higher heat transfer rates.


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