Page 410 - Mechanical Engineers' Handbook (Volume 4)
P. 410

2 Heat-Transfer Correlations for Electronic Equipment Cooling  399






















                           Figure 12 Recommended curve for estimation of heat-transfer coefficient for fluids flowing normal to
                           staggered tubes 10 rows deep (from Ref. 22).



                              For staggered prismatic components, Eq. (65) may be modified to 29
                                    Nu   0.446       Re           1   0.639
                                                              0.57
                                                                                      0.172
                                                                                   d
                                                                             S
                                                                              T
                                               (1/6)   (5A /A )             S T,max  S L        (66)
                                                         n
                                                           0
                           where d is the prism side dimension, S is the longitudinal separation, S is the transverse
                                                          L
                                                                                     T
                           separation, and S T,max  is the maximum transverse spacing if different spacings exist.
                              When cylindrical heat sources are encountered in electronic equipment, a modification
                           of Eq. (57) has been proposed :
                                                   30
                                                                   	Vd
                                                          hd   FB       n

                                                     Nu                                         (67)
                                                          k  ƒ
                           where F is an arrangement factor depending on the cylinder geometry (see Table 10) and
                           where the constants B and n are given in Table 11.
                           Table 10 Values of F to Be Used in Eq. (67) a
                           Single cylinder in free stream: F   1.0
                           Single cylinder in duct: F   1   d/w
                           In-line cylinders in duct:
                           F   1      1    1     1      1.81  1.46   0.318 [Re    0.526 (0.354 / S ) ]
                                                0.872
                                            S L  S L   S T  S T
                                   	 S T          2     2                       T
                           Staggered cylinders in duct:
                           F   1      1    1         16.80   4.15         15.33   3.69
                                            1 15.50
                                                                  1 14.15
                                                                                        0.13
                                            S L  S T  S T         S L  S T  S T
                                   	 S T         2                    2               Re
                           a
                           Re to be evaluated at film temperature. S L   ratio of longitudinal spacing to cylinder diameter. S T   ratio of transverse
                           spacing to cylinder diameter.
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