Page 262 - Fluid Mechanics and Thermodynamics of Turbomachinery
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Radial Flow Gas Turbines  243
                          From the design point velocity triangles, Figure 8.3,
                                                                                 2
                              c 2 D U 2 cosec a 2 ,w 3 D U 3 cosec ˇ 3 ,c 3 D U 3 cot ˇ 3 ,W D U .
                                                                                 2
                          Thus substituting all these expressions in eqn. (8.8) and noting that U 3 D U 2 r 3 /r 2 ,
                          then
                                   "     (                                          )#  1
                                                                2
                                        1    T 3    2       r 3         2       2
                                ts D 1 C     N  cosec ˛ 2 C     .  R cosec ˇ 3 C cot ˇ 3 /  (8.9)
                                        2
                                             T 2            r 2
                                                                                         1
                          Usually r 3 and ˇ 3 are taken to apply at the arithmetic mean radius, i.e. r 3 D .r 3t C
                                                                                         2
                          r 3h /. The temperature ratio .T 3 /T 2 / in eqn. (8.9) can be obtained as follows.
                            At the nominal design condition, referring to the velocity triangles of Figure 8.3,
                                     2
                                2
                          w 2  U D c , and so eqn. (8.2) can be rewritten as
                           3    3    3
                                                   2
                                               2
                                       1
                                  h 3 D .U 2  w C c /.                                    (8.2a)
                              h 2         2    2   3
                                       2
                                                                      1  2
                          This particular relationship, in the form I 2 D h 02 rel  U D h 03 can be easily iden-
                                                                      2  2
                          tified in Figure 8.4.
                            Again, referring to the velocity triangles, w 2 D U 2 cot a 2 and c 3 D U 3 cot ˇ 3 ,a
                          useful alternative form to eqn. (8.2a) is obtained,
                                                                 2
                                          2
                                                  2
                                       1
                              h 2  h 3 D U [.1  cot a 2 / C .r 3 /r 2 / cot ˇ 3 ],        (8.2b)
                                       2  2
                          where U 3 is written as U 2 r 3 /r 2 . For a perfect gas the temperature ratio T 3 /T 2 can
                          be easily found. Substituting h D C p T D 
RT/.
  1/ in eqn. (8.2b)
                                                  "                       #
                                                                    2
                                           .
  1/
                                  T 3  1  2              2      r 3    2
                              1      D U  2        1  cot ˛ 2 C      cot ˇ 3
                                       2
                                  T 2       
RT 2               r 2
                                                         "                        #
                                                         2                  2
                                ∴  T 3  D 1  1 .
  1/  U 2  1  cot ˛ 2 C  r 3  cot ˇ 3 ,  .8.2c/
                                                                               2
                                                                2
                                           2
                                  T 2               ˛ 2                 r 2
                          where a 2 D .
RT 2 / 1/2  is the sonic velocity at temperature T 2 .
                            Generally this temperature ratio will only have a very minor effect upon the
                          numerical value of   ts and so it is often ignored in calculations. Thus,
                                   "     (                                           )#  1

                                                              2
                                                                      2
                                                  2
                                                                                2
                                ts ' 1 C  1    N cosec ˛ 2 C  r 3av  .  R cosec ˇ 3av C cot ˇ 3av /  (8.9a)
                                        2
                                                          r 2
                          is the expression normally used to determine the total-to-static efficiency. An alter-
                          native form for   ts can be obtained by rewriting eqn. (8.6) as
                                                    h 3ss /     h 3 /     h 3s /      h 3ss /
                                   h 01  h 03  .h 01      .h 03      .h 3       .h 3s
                                ts D        D
                                   h 01  h 3ss                 .h 01  h 3ss /
                                              2
                                        2
                                                     2
                                 D 1  .c C   N c C   R w //c 2                            .8.10/
                                        3     2      3  0
                          where the spouting velocity c 0 is defined by,
                                         1 2
                                   h 3ss D c D C p T 01 [1  .p 3 /p 01 / .
 1//
  ]       (8.11)
                              h 01
                                         2 0
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