Page 253 - Mechanical Engineers' Handbook (Volume 4)
P. 253

242   Furnaces

                             Charts have been prepared by Gurney-Lurie, Heisler, Hottel, and others showing values
                          for Y and Y for various R factors as a function of X. Separate charts are provided for Y s
                              s
                                   c
                          and Y , with a series of curves representing a series of values of R. These curves are straight
                              c
                          lines for most of their length, curving to intersect at Y   1 and X   0. If straight lines are
                          extended to Y   1, the curves for Y at all values of R converge at a point near X   0.1 on
                                                      c
                          the line for Y   1. It is accordingly possible to prepare a single line chart for  ln Y /(X
                                                                                            c
                                    c
                          0.1) to fit selected geometrical shapes. This has been done in Fig. 23 for slabs, long cylinders,
                          and spheres. Values of Y determined with this chart correspond closely with those from
                                              c
                          conventional charts for X   0.1 greater than 0.2.
                             Because the ratio Y /Y remains constant as a function of R after initial heating, it can
                                               c
                                             s
                          be shown in chart form, as in Fig. 24, to allow Y to be determined after Y has been found.
                                                                s
                                                                                    c
                             By way of illustration, a carbon steel slab 8 in. thick is being heated from cold to T
                                                                                               s
                          2350 F in a furnace with a constant wall temperature of 2400 F, with a view factor of 1 and
                          a mean emissivity–absorptivity factor of 0.80. The desired final temperature of the unheated
                          surface is 2300 F, making the Y factor
                                                   c
                                                       2400   2300
                                                  Y                 0.0429
                                                   c
                                                        2400   70
                                                             8
                          From Fig. 23 H   114   0.80   91; r   ⁄12   0.67; R is assumed at 17. The required
                                      r
                          heating time is determined from Fig. 24:
                                                           17
                                                    R              0.279
                                                        0.67   91
                                                          ln Y c
                                                        X   0.1    1.7
                          and

























                                        Figure 23 A plot of  ln Y c /(X   0.1) as a function of R. 1
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