Related articles in HEDH:

1. Plate heat exchangers:

1. advantages and limitations of, 3.7.1-1 - 3.7.1-2

2. condensing/boiling in, 3.7.3-5

3. corrugation design, 3.7.1-4 - 3.7.1-5

4. costing 4.8.1-8 - 4.8.1-9

1. comparison of costs with those for shell-and-tube heat exchangers, 4.8.1-8 - 4.8.1-9

5. costing 4.8.4-1 - 4.8.4-2

6. description, 3.1.2-4 - 3.1.2-6

1. gasketed plate, 3.1.2-4

2. lamella (Ramen), 3.1.2-5

7. distribution of flowin, 3.7.2-2

8. entry loss in, 3.7.2-2

9. factors affecting plate specification, 3.7.2-1 - 3.7.2-2

1. corrugation geometry, 3.7.2-1 - 3.7.2-2

2. distribution, 3.7.2-2

10. fouling in, 3.7.3-4 - 3.7.3-5

11. heat transfer and pressure drop in, 3.7.3-1 - 3.7.3-4

12. mechanical design, 4.4.2-1 - 4.4.2-5

1. brazed plate design, 4.4.2-5

2. double-wall gasketed plates, 4.4.2-4

3. frame design, 4.4.2-3 - 4.4.2-4

4. gasket design and properties, 4.4.2-3

5. plate construction features, 4.4.2-2 - 4.4.2-4

6. plate design features, 4.4.2-2 - 4.4.2-3

7. welded pair plate, 4.4.2-4

8. welded plate, 4.4.2-5

13. multiple duties in, 3.7.1-2

14. Packinox, 3.1.2-5 - 3.1.2-6

15. pass arrangement in, 3.7.2-5 - 3.7.2-7

16. performance calculations for, 3.7.3-5 - 3.7.3-7

17. plate arrangements and correction factors for, 3.7.2-5 - 3.7.2-8

1. concurrency corrections, 3.7.2-5 - 3.7.2-6

2. distribution along port manifolds, 3.7.2-7

3. end effects, 3.7.2-6 - 3.7.2-7

4. types of pass arrangements, 3.7.2-5

18. plate design, overall in, 3.7.2-2 - 3.7.2-3

1. NTU rating, 3.7.2-2 - 3.7.2-3

2. performance characteristics, 3.7.2-3

19. port arrangements in, 3.7.2-2

20. shell-encased, 4.4.2-5

21. specifications, 4.9.2-5

22. spiral plate, 3.1.2-4 - 3.1.2-5

23. thermal mixing in, 3.7.2-3 - 3.7.2-5

1. characteristics of, as packings for fixed beds, 2.2.5-2

2. direct-contact condensation on films flowing on, 3.20.3-1 - 3.20.3-3

3. parallel, laminar heat transfer in flow between

1. in laminar flow, 2.5.1-9 - 2.5.1-13

2. in turbulent flow, 2.5.1-13