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Handbook of Turbomachinery Second Edition Revised - Ventech!

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were superior to both 908 discrete ribs and parallel-angled continuous ribs<br />

and were recommended for internal cooling passage designs. For 608 and<br />

458, parallel discrete ribs had higher ribbed wall heat transfer, lower smooth<br />

wall heat transfer, and lower channel pressure drop than parallel full ribs.<br />

Parallel 608 discrete ribs had the highest ribbed wall heat transfer, and<br />

parallel 308 discrete ribs caused the lowest pressure drop. The heat transfer<br />

and pressure drops in crossed-angled continuous and discrete rib cases were<br />

all lower than those in the corresponding 908 and parallel-angled rib cases.<br />

Crossed arrays <strong>of</strong> angled ribs had poor thermal performance and were not<br />

recommended. Correlations <strong>of</strong> Stanton number and friction factor are<br />

provided for turbine-cooling design.<br />

More recent work by Han et al. [76] has studied the effects <strong>of</strong> ribs with<br />

different configurations and channel orientation on heat transfer for a<br />

rectangular channel with width-to-depth aspect ratio about 2:1. The local<br />

heat-transfer coefficient distribution in a rotating frame is different from<br />

that <strong>of</strong> a stationary frame. Heat-transfer coefficient patterns in radial<br />

outward flow and radial inward flow conditions show different dependence<br />

on rotation. This is primarily due to the reversal <strong>of</strong> the Coriolis force acting<br />

on the moving fluid in a rotating flow. The results <strong>of</strong> this study confirm a<br />

similar heat-transfer effect in a two-pass rotating rectangular channel as is<br />

observed in a two-pass rotating square channel from the previous work. In<br />

general, the rib-roughened surfaces in a rectangular channel perform<br />

similarly to smooth surfaces with increasing rotational speed. However, the<br />

average heat-transfer coefficient magnitude in a rectangular channel with<br />

ribbed wall is much higher than that <strong>of</strong> the smooth walls. Ribs placed at an<br />

angle to the bulk flow direction induce greater heat-transfer enhancement.<br />

Comparative studies suggest that a 458 parallel rib configuration in a<br />

rectangular channel is more suitable to enhance heat transfer than a 458<br />

cross configuration for both nonrotating and rotating cases. The effect <strong>of</strong><br />

channel orientation on heat transfer shows that a 908 channel orientation<br />

has more effect on leading and trailing surfaces than a 1358 orientation due<br />

to rotation. The difference in Nusselt number ratios between trailing and<br />

leading surfaces in a smooth channel is smaller in a 1358 channel orientation<br />

than a 908 channel orientation. Han et al. [77] studied the heat-transfer and<br />

friction performance <strong>of</strong> a square channel with parallel, crossed, and Vshaped<br />

angled ribs. Nine rib configurations were tested: 908 rib; 608 and 458<br />

parallel ribs; 608 and 458 crossed ribs; 608 and 458 V-shaped ribs; and 608<br />

and 458 A-shaped ribs. The results showed that the 608/458 V-shaped rib<br />

performed better than the 608/458 parallel rib, and better than the 608/458<br />

crossed rib and the 908 rib. The V-shaped rib produced the highest heattransfer<br />

augmentation, while the A-shaped rib generated the greatest<br />

Copyright © 2003 Marcel Dekker, Inc.

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