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F and θ charts for shell-and-tube exchangers
DOI 10.1615/hedhme.a.000106
1.5 MEAN TEMPERATURE DIFFERENCE
1.5.2 F and θ charts for shell-and-tube exchangers
J. Taborek
In this Section are presented sets of equations and graphs for simple heat exchanger configurations and for a set of shell-and-tube exchangers defined using the nomenclature of the TEMA Handbook. Descriptive material, comments on proper usage and limiting points are also included with each specific configuration. The topics covered are:
| A. | Counter Flow | Figure 1 |
| B. | Co-current Flow | Figure 2 |
| C. | TEMA E shell-and-tube | |
| flow arrangements | ||
| E-shell, 1-2N | Figure 3 | |
| E-shell, 2 in series | Figure 4 | |
| E-shell, 3 in series | Figure 5 | |
| E-shell, 4 in series | Figure 6 | |
| E-shell, 5 in series | Figure 7 | |
| E-shell, 6 in series | Figure 8 | |
| D. | E-shell, 3 tube passes | Figure 9 |
| E. | J-shell, one tube pass | Figure 10 |
| 2N tube passes | Figure 11 | |
| F. | G-shell, 2N tube passes | Figure 12 |
| G. | F-shell, partition thermal leakage | Figure 13 |
The reader should refer to Section 105 for a description of the terms involved.
A. Countercurrent flow (Figure 1)
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