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104 Fluid Mechanics, Thermodynamics of Turbomachinery












                                     FIG. 4.8. Velocity diagram for 100% reaction turbine stage.

                          will be observed have a dramatic increase in blade profile loss, has R/  decreasing
                          from zero to  0.25 in the same range of incidence.
                            It was shown above that negative values of reaction indicated diffusion of the
                          rotor relative velocity (i.e. for R< 0, w 3 <w 2 ). A similar condition which holds
                          for diffusion of the nozzle absolute velocity is, that if R> 1, c 2 <c 1 .
                            Substituting tan ˇ 3 D tan ˛ 3 C U/c x into eqn. (4.22b) gives

                                      c x
                              R D 1 C    .tan ˛ 3  tan ˛ 2 /.                            (4.22c)
                                      2U
                          Thus, when ˛ 3 D ˛ 2 , the reaction is unity (also c 2 D c 3 ). The velocity diagram for
                          R D 1 is shown in Figure 4.8 with the same values of c x , U and W used for R D 0
                                  1
                          and R D . It will be apparent that if R exceeds unity, then c 2 <c 1 (i.e. nozzle flow
                                  2
                          diffusion).
                            EXAMPLE 4.2. A single-stage gas turbine operates at its design condition with
                          an axial absolute flow at entry and exit from the stage. The absolute flow angle at
                          nozzle exit is 70 deg. At stage entry the total pressure and temperature are 311 kPa
                          and 850 ° C respectively. The exhaust static pressure is 100 kPa, the total-to-static
                          efficiency is 0.87 and the mean blade speed is 500 m/s.
                            Assuming constant axial velocity through the stage, determine

                           (i) the specific work done;
                          (ii) the Mach number leaving the nozzle;
                          (iii) the axial velocity;
                          (iv) the total-to-total efficiency;
                           (v) the stage reaction.

                            Take C p D 1.148 kJ/(kg ° C) and 
 D 1.33 for the gas.
                            Solution. (i) From eqn. (4.10), total-to-static efficiency is
                                                       W
                                   h 01  h 03
                                ts D        D                .
 1//
  .
                                   h 01  h 3ss  h 01 f1  .p 3 /p 01 /  g
                          Thus, the specific work is

                              W D   ts C p T 01 f1  .p 3 /p 01 / .
 1//
 g
                                  D 0.87 ð 1148 ð 1123 ðf1  .1/3.11/ 0.248 g

                                  D 276 kJ/kg.
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