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A B C D E F G H I J K L M N O P Q R S T U V W X Y Z
J-type shells, in shell-and-tube heat exchangers:
calculation of heat transfer and pressure drop in, temperature difference correction (F) and ?-NTU charts for,
F and θ charts for shell-and-tube exchangers
Jackets, PD5500 guidelines for, Jackson, J D Jacob number, Jacobs, H R Japan, guide to national practice for heat exchanger mechanical design: Jayatillaka relation, between heat and momentum transfer, Jens and Lottes correlation for subcooled forced convective boiling of water, Jet impingement dryer, Jets: Joback methods Jones, A E,

Index

HEDH
A B C D E F G H I J
J-type shells, in shell-and-tube heat exchangers:
calculation of heat transfer and pressure drop in, temperature difference correction (F) and ?-NTU charts for,
F and θ charts for shell-and-tube exchangers
Jackets, PD5500 guidelines for, Jackson, J D Jacob number, Jacobs, H R Japan, guide to national practice for heat exchanger mechanical design: Jayatillaka relation, between heat and momentum transfer, Jens and Lottes correlation for subcooled forced convective boiling of water, Jet impingement dryer, Jets: Joback methods Jones, A E,
K L M N O P Q R S T U V W X Y Z
J J-type shells, in shell-and-tube heat exchangers: temperature difference correction (F) and ?-NTU charts for,
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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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