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                       230                       Applied Process Design for Chemical and Petrochemical Plants

                       steel, aluminum, aluminum bronze, stainless steel, admi-  can be fabricated with more than one finned tube in a larger
                       ralty, copper, copper-nickel, monel, and chrome moly alloy.  shell. The fins are more effective or beneficial when the fin-
                         This longitudinal fin style unit can be used in cross-  side film coefficient is lower than the inside tube coefficient;
                       exchange, kettle-type reboilers, chillers, and condensers.  therefore, the poorest heat transfer fluid conditions are best
                       The rating/design of longitudinal finned tubes is presented  used on the finned side of the tube.
                       by Brown Fintube Co. in an unnumbered bulletin, refer-
                       ence 211. The double pipe finned tube, Figure 10-4A, is  Finned Side Heat Transfer
                       often applicable for gas, viscous liquids, or small volumes,
                       and the economics favor high operating pressure due to the  For a double pipe exchanger (one finned tube in each of
                       small diameter shell. 211  They operate well in dirty or some-  two shells), see Figure 10-4A, the heat flow resistances are 211
                       what fouling conditions due to the ease of cleaning. Units
                                                                               a. Film resistances on outside of the tube, h o .

                                                                               b. Metal tube wall resistance, R m
                                                                               c. Film resistance on inside of tube, h i .
                                                                               d. Note that fouling resistance on tube finned side and
                                                                                 inside tube must be added.

                                                                                                                         (10-248)
                                                                             1>U o      1>h o   	  1>h i   	  R m
                                                                                                     2
                                                                             where U o , h o , h i   Btu/(hr) (ft )(°F)
                                                                                       2
                                                                             R m   (hr)(ft ) (°F)/BTU
                                                                               e. See Table 10-41 for suggested overall U coefficients and
                                                                                 Table 10-42 for mechanical data.

                                                                               Figure 10-46 gives the usual Sieder-Tate chart and equa-
                                                                             tion for tube-side, bare-tube heat transfer. For the finned
                                                                             shell-side heat transfer, see Figures 10-153A, 10-153B,
                                                                             10-153C 211  or the recommendation of Kern and Kraus, 206
                                                                             Figure 10-154.


                       Figure 10-152A. Typical longitudinal finned tubes. Uninterrupted and
                       Interrupted G-Fin ®  Tubes. (Used by permission: Griscom-Russell,
                       Ecolaire Corp.) (Also see Figure 10-4A(3).)




























                       Figure 10-152B. Typical longitudinal finned tubes. Relative pipe sizes and number of longitudinal fins. (Used by permission: Griscom-Russell,
                       Ecolaire Corp.) (Also see Figure 10-4A(3).)
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