Electrochemical study of mass transfer in decaying annular swirl flow Part II: Correlation of mass transfer data

1995 ◽  
Vol 25 (1) ◽  
Author(s):  
S. Yapici ◽  
M.A. Patrick ◽  
A.A. Wragg
1994 ◽  
Vol 24 (7) ◽  
pp. 685-693 ◽  
Author(s):  
S. Yapici ◽  
M. A. Patrick ◽  
A. A. Wragg

1972 ◽  
Vol 94 (1) ◽  
pp. 23-28 ◽  
Author(s):  
E. Brundrett ◽  
W. B. Nicoll ◽  
A. B. Strong

The van Driest damped mixing length has been extended to account for the effects of mass transfer through a porous plate into a turbulent, two-dimensional incompressible boundary layer. The present mixing length is continuous from the wall through to the inner-law region of the flow, and although empirical, has been shown to predict wall shear stress and heat transfer data for a wide range of blowing rates.


Author(s):  
Florian Wassermann ◽  
Sven Grundmann ◽  
Michael Kloss ◽  
Heinz-Peter Schiffer

Cyclone cooling is a promising method to enhance heat-transfer processes in future internal turbine-blade leading-edge cooling-ducts. The basic component of such cooling channels is the swirl generator, which induces a swirling movement of the coolant. The angular momentum generates stable, complex and three-dimensional flow structures of helical shape with alternating axial flow directions. Full three-dimensional and three-component velocity measurements using magnetic resonance velocimetry (3D3C-MRV) were conducted, with the aim to understand the complex structure of pipe flows with strong swirl. In order to mimic the effect of different installation concepts of the cyclone-cooling ducts an idealized bend-duct swirl-tube configuration with variable exit orifices has been investigated. Pronounced helical flow structures and distinct velocity zones could be found in this swirl flow. One substantial result is the identification of stationary helix-shaped streaks of high axial velocity in the direct vicinity of the wall. These findings are in good agreement with mass-transfer measurements that also show helix-shaped structures with increased mass transfer at the inner surface of the tube. According to the Reynolds analogy between heat and mass transfer, augmented heat-transfer processes in these areas are to be expected.


1975 ◽  
Vol 2 (4) ◽  
pp. 351-357 ◽  
Author(s):  
A. Caprani ◽  
C. Deslouis ◽  
I. Epelboin ◽  
B. Tribollet

1987 ◽  
Vol 17 (2) ◽  
pp. 385-397 ◽  
Author(s):  
Y. Iwadate ◽  
M. Lassouani ◽  
F. Lantelme ◽  
M. Chemla

1984 ◽  
Vol 23 (4) ◽  
pp. 510-512 ◽  
Author(s):  
Stanislaw Ledakowicz ◽  
Hubert Nettelhoff ◽  
Wolf Dieter Deckwer

1990 ◽  
Vol 112 (3) ◽  
pp. 216-222 ◽  
Author(s):  
James R. Fair

Energy from hot gas discharge streams can be recovered by transfer directly to a coolant liquid in one of several available gas-liquid contacting devices. The design of the device is central to the theme of this paper, and experimental work has verified that the analogy between heat transfer and mass transfer can be used for design purposes. This enables the large amount of available mass transfer data for spray, packed, and tray columns to be used for heat transfer calculations. Recommended methods for designing the several types of gas-liquid contacting device are summarized.


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