1. in air-cooled heat exchangers, 3.8.6-1
2. in condensers, 3.4.7-1 - 3.4.7-2
3. in double-pipe heat exchangers, 3.2.2-4
4. in evaporators,/ 3.5.6-1 - 3.5.6-2
5. in fluidized beds, 2.2.6-2 - 2.2.6-3
6. in foam systems, 2.12.1-3 - 2.12.1-4
7. in gas-liquid flow, 2.3.2-7 - 2.3.2-18
1. frictional, in straight pipes, 2.3.2-9 - 2.3.2-12
2. in shell-and-tube heat exchangers, 2.3.2-12 - 2.3.2-13
3. in singularities, 2.3.2-15 - 2.3.2-18
8. in headers, nozzles, and turnarounds in shell-and-tube heat exchangers, 2.2.7-1 - 2.2.7-11
9. in helical coils of rectangular cross section, 2.5.15-6 - 2.5.15-7
10. in internally finned tubes, 2.5.11-2 - 2.5.11-3
11. in liquid-liquid flow, 2.3.5-1 - 2.3.5-40
13. in microchannels
1. in condensation in, 2.13.6-5 - 2.13.6-19
2. in evaporation in, 2.13.4-16 - 2.13.4-19
14. in multiphase systems, 2.3.1-1 - 2.3.1-10
15. overall, in cooling towers, 3.12.2-6 - 3.12.2-9
16. in packings of cooling towers, 3.12.2-7 - 3.12.2-8
17. in plate fin heat exchangers, 3.9.10-1 - 3.9.10-2
18. in plate heat exchangers, 3.7.3-1 - 3.7.3-4
19. and pumping power in heat exchangers, 1.2.4-5 - 1.2.4-6
20. in reboilers, 3.6.3-1
21. on shell side of shell-and-tube heat exchangers, 3.3.1-1 - 3.3.11-5
22. on the shell side of twisted tube heat exchangers:
1. longitudinal flow (straight twisted tubes), 3.23.3-1 - 3.23.3-6
2. longitudinal flow (twisted bundle), 3.23.3-6 - 3.23.3-7
3. cross flow, 3.23.3-7 - 3.23.3-10
23. in single-phase systems: ducts and fittings, 2.2.2-1 - 2.2.2-28