1. Fins (see also Extended surfaces):
1. application in enhancement of boiling heat transfer, 2.7.9-1 - 2.7.9-40
2. as augmentation devices, 2.5.11-5 - 2.5.11-6
3. in condensation 2.6.6-9 - 2.6.6-13
4. internally finned tubes 2.5.11-2 - 2.5.11-3
5. internally finned tubes 2.6.6-17
3. on cylinders in tube banks: pressure drop in, 2.2.4-13 - 2.2.4-14
4. description of types, 2.4.9-3 - 2.4.9-5
5. effect on flow over cylinders, 2.2.3-7
6. free convective heat transfer from, 2.5.7-25
7. longitudinal (straight): application in double-pipe heat
2. exchangers, 3.2.1-1 - 3.2.6-2
3. efficiency of 2.4.9-5 - 2.4.9-8
4. efficiency of 3.2.1-1 - 3.2.6-2
8. low finned tubes: applications in shell-and-tube heat exchangers, 3.3.11-2 - 3.3.11-4
1. description of, 2.4.9-3 - 2.4.9-4
2. correlation for single-phase heat transfer in flow over, 2.5.3-12 - 2.5.3-13
3. in longitudinal flow in tube banks, 3.3.12-12 - 3.3.12-13
9. radiating, 2.9.8-6 - 2.9.8-7
10. single-phase forced convective heat transfer to banks of tubes with, 2.5.3-19 - 2.5.3-30
1. efficiency of fins in 2.4.9-5 - 2.4.9-30
2. efficiency of fins in 2.5.3-19 - 2.5.3-20
3. experimental data compared with correlations for, 2.5.3-21 - 2.5.3-23
4. heat transfer correlations for high fins, 2.5.3-21 - 2.5.3-26
5. heat transfer correlations for low fins, 2.5.3-26 - 2.5.3-28
11. thermal contact resistance with, 2.4.6-5 - 2.4.6-6
12. types, in heat exchangers, 1.1.4-1
13. types used in air-cooled heat exchangers, 3.8.3-1 - 3.8.3-3