Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Rossby numbers in turbulent rotating Rayleigh-Bénard convection are presented. For relatively small Ra $\approx 10^8$ and large Pr modest rotation can enhance the heat transfer by up to 30%. At larger Ra there is less heat-transfer enhancement, and at small Pr≲0.7 there is no heat-transfer enhancement at all. We suggest that the small-Pr behavior is due to the breakdown of the heat-transfer-enhancing Ekman pumping because of larger thermal diffusion
Numerical data for the heat transfer as a function of the Prandtl (Pr) and Rossby (Ro) numbers in tu...
Numerical data for the heat transfer as a function of the Prandtl (Pr)and Rossby (Ro) numbers in tur...
For given aspect ratio and given geometry, the nature of Rayleigh Benard convection (RBC) is determi...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
For given aspect ratio and given geometry, the nature of Rayleigh Benard convection (RBC) is determi...
Numerical data for the heat transfer as a function of the Prandtl (Pr) and Rossby (Ro) numbers in tu...
Numerical data for the heat transfer as a function of the Prandtl (Pr) and Rossby (Ro) numbers in tu...
Numerical data for the heat transfer as a function of the Prandtl (Pr)and Rossby (Ro) numbers in tur...
For given aspect ratio and given geometry, the nature of Rayleigh Benard convection (RBC) is determi...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh, Prandtl, and Ro...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
Experimental and numerical data for the heat transfer as a function of the Rayleigh-, Prandtl-, and ...
For given aspect ratio and given geometry, the nature of Rayleigh Benard convection (RBC) is determi...
Numerical data for the heat transfer as a function of the Prandtl (Pr) and Rossby (Ro) numbers in tu...
Numerical data for the heat transfer as a function of the Prandtl (Pr) and Rossby (Ro) numbers in tu...
Numerical data for the heat transfer as a function of the Prandtl (Pr)and Rossby (Ro) numbers in tur...
For given aspect ratio and given geometry, the nature of Rayleigh Benard convection (RBC) is determi...