Taylor-Couette-Poiseuille Flow Heat Transfer Experimental Data

UQ eSpace ◽  
2020 ◽  
Author(s):  
Ingo Jahn ◽  
Phillip Swann ◽  
Hugh Russell
Keyword(s):  
Heat Transfer ◽  
Experimental Data ◽  
Poiseuille Flow ◽  
Flow Heat ◽  
Taylor Couette

Taylor-Couette-Poiseuille flow and heat transfer in an annular channel with a slotted rotor

2017 ◽  
Vol 112 ◽  
pp. 92-103 ◽  
Author(s):  
Nicolas Lancial ◽  
Federico Torriano ◽  
François Beaubert ◽  
Souad Harmand ◽  
Gilles Rolland
Keyword(s):  
Heat Transfer ◽  
Poiseuille Flow ◽  
Annular Channel ◽  
Flow And Heat Transfer ◽  
Taylor Couette

Effect of radial injection on heat transfer of a Taylor–Couette–Poiseuille flow

2020 ◽  
Vol 77 (3) ◽  
pp. 271-285
Author(s):  
Mahdi Farsi ◽  
Sina Karbalaee M. ◽  
Farshad Kowsary ◽  
Pedram Hanafizadeh
Keyword(s):  
Heat Transfer ◽  
Poiseuille Flow ◽  
Radial Injection ◽  
Taylor Couette

Application of a Zonal K-ε Model on Simulation of Turbulent Mixed Convection

2010 ◽  
Author(s):  
Mehdi Shahraeeni ◽  
Mehrdad Raisee
Keyword(s):  
Heat Transfer ◽  
Experimental Data ◽  
Buoyancy Force ◽  
Turbulence Modeling ◽  
Quantitative Agreement ◽  
Constant Heat Flux ◽  
Vertical Tube ◽  
Numerical Results ◽  
Flow Heat ◽  
Sudden Decrease

Fluid flow and heat transfer in a vertical tube under constant heat flux have been studied and effect of buoyancy force on the heat transfer coefficient is investigated. The finite volume method is used to study turbulent flow in both upward and downward directions. For the turbulence modeling, a zonal k-e model is employed and the numerical results are compared with available experimental data. The results of the simulation show that for the downward flow, heat transfer is enhanced and for strong buoyancy force, flow reversal is observed. In contrast, for the heated upward flow, heat transfer can be either impaired or enhanced by the buoyancy force depending on its strength. Partial laminarization is caused by the buoyancy in the case of modest buoyancy force. For the condition of stronger buoyancy force, a sudden decrease in the fully-developed Nusselt number is evident in the experimental data and well predicted by the numerical solution. In general, the quantitative agreement between the numerical results and the experimental data is satisfactory.

Convective Heat Transfer to Turbulent Droplet Flow in Circular Tubes

1981 ◽  
Vol 103 (4) ◽  
pp. 679-684 ◽  
Author(s):  
A. G. Rane ◽  
Shi-Chune Yao
Keyword(s):  
Heat Transfer ◽  
Experimental Data ◽  
Single Phase ◽  
Size Variation ◽  
Number Density ◽  
Droplet Flow ◽  
Dimensionless Groups ◽  
Flow Heat ◽  
Thermal Entrance ◽  
Good Agreement

Turbulent droplet flow heat transfer is analyzed for the thermal entrance region of a circular tube. Calculations are performed considering droplet size variation, vapor acceleration and dilution of droplet number density until the single-phase fully developed conditions is reached. Effect of the relevant dimensionless groups on the heat transfer results is studied. The analytical results are compared with the available experimental data. These comparisons show good agreement between the experimental data and the predictions.

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