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Nozzle energy equation and nozzle efficiency

Short answer

Steady adiabatic nozzle energy equation: h01 = h2 + C2^2/2, giving C2 = sqrt(2(h01 - h2)). Nozzle efficiency eta_n = (h01 - h2)/(h01 - h2s) = C2^2/C2s^2. Velocity coefficient C_v = C2/C2s = sqrt(eta_n); discharge coefficient C_d = m_dot_actual / m_dot_ideal. Loss appears as higher exit temperature T2 > T2s and lower total pressure p02 < p01 on the T-s diagram.

Write the energy equation for a gas nozzle and derive an expression for the exit velocity. Define nozzle efficiency, velocity coefficient and discharge coefficient and show how the loss appears on a T-s diagram.

Energy equation

For steady adiabatic flow with no shaft work, per unit mass (inlet 1, exit 2):

h1+C122=h2+C222h_1 + \frac{C_1^2}{2} = h_2 + \frac{C_2^2}{2}

so the exit velocity is

C2=2(h1−h2)+C12=2(h01−h2)C_2 = \sqrt{2(h_1 - h_2) + C_1^2} = \sqrt{2(h_{01} - h_2)}

For a perfect gas with negligible inlet velocity and an isentropic process 1-2s:

C2s=2cpT1[1−(p2p1)(γ−1)/γ]C_{2s} = \sqrt{2c_p T_1\left[1 - \left(\frac{p_2}{p_1}\right)^{(\gamma-1)/\gamma}\right]}

T-s diagram

 T
 |  1 ------ p1
 |  |\
 |  | \
 |  |  \ p2
 |  2s  2   <- 2 is at higher T than 2s
 |
 +--------------- s

Friction heats the gas, so the actual exit state 2 has a higher enthalpy than 2s and less kinetic energy is produced.

Efficiency and coefficients

  • Nozzle efficiency: ratio of actual kinetic-energy gain to the isentropic gain between the same pressures.
ηn=h01−h2h01−h2s=C22/2C2s2/2≈T01−T2T01−T2s\eta_n = \frac{h_{01} - h_2}{h_{01} - h_{2s}} = \frac{C_2^2/2}{C_{2s}^2/2} \approx \frac{T_{01} - T_2}{T_{01} - T_{2s}}
  • Velocity coefficient: Cv=C2C2s=ηnC_v = \dfrac{C_2}{C_{2s}} = \sqrt{\eta_n}. Typical values 0.95 to 0.99 give ηn≈0.90\eta_n \approx 0.90 to 0.98.
  • Coefficient of discharge: Cd=m˙actualm˙idealC_d = \dfrac{\dot m_{actual}}{\dot m_{ideal}}, usually 0.95 to 0.99 for convergent nozzles, reduced by boundary layer blockage.
  • Nozzle loss coefficient: ζ=h2−h2sC22/2\zeta = \dfrac{h_2 - h_{2s}}{C_2^2/2}, where h2−h2s=(1−ηn)(h01−h2s)h_2 - h_{2s} = (1 - \eta_n)(h_{01} - h_{2s}).

The nozzle losses come from skin friction, mixing and separation, and, in a supersonic nozzle, from shock waves and over- or under-expansion. The total temperature is unchanged in the actual process, but total pressure falls: p02<p01p_{02} < p_{01}.

✓ Answer checked by Claude Opus 5.5 (high effort)

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