---
title: "Nozzle energy equation and nozzle efficiency"
subject: "Turbo Machines"
chapter: 4
key: "semester_7/turbo_machines:nozzle-energy-equation-efficiency"
source: https://www.bctengineer.com/q/semester_7/turbo_machines/nozzle-energy-equation-efficiency
site: BCT Engineering
---

# Nozzle energy equation and nozzle efficiency

Turbo Machines · Chapter 4: Gas Turbine Nozzles

- Asked in: year not given, 6 marks
- Answer checked by Claude Opus 5.5 (high effort) on 2026-10-14
- Page: https://www.bctengineer.com/q/semester_7/turbo_machines/nozzle-energy-equation-efficiency
- Whole chapter: https://www.bctengineer.com/md/semester_7/turbo_machines/chapter-4

## Question

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.

## 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.

## Answer

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

$$
h_1 + \frac{C_1^2}{2} = h_2 + \frac{C_2^2}{2}
$$

so the exit velocity is

$$
C_2 = \sqrt{2(h_1 - h_2) + C_1^2} = \sqrt{2(h_{01} - h_2)}
$$

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

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

#### T-s diagram
```text
 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.

$$
\eta_n = \frac{h_{01} - h_2}{h_{01} - h_{2s}} = \frac{C_2^2/2}{C_{2s}^2/2} \approx \frac{T_{01} - T_2}{T_{01} - T_{2s}}
$$

- **Velocity coefficient:** $C_v = \dfrac{C_2}{C_{2s}} = \sqrt{\eta_n}$. Typical values 0.95 to 0.99 give $\eta_n \approx 0.90$ to 0.98.
- **Coefficient of discharge:** $C_d = \dfrac{\dot m_{actual}}{\dot m_{ideal}}$, usually 0.95 to 0.99 for convergent nozzles, reduced by boundary layer blockage.
- **Nozzle loss coefficient:** $\zeta = \dfrac{h_2 - h_{2s}}{C_2^2/2}$, where $h_2 - h_{2s} = (1 - \eta_n)(h_{01} - h_{2s})$.

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: $p_{02} < p_{01}$.

## Check yourself

The answer's key points as multiple-choice questions, with the correct option and why.

1. For a steady adiabatic nozzle with no shaft work, the exit velocity is
   A. C2 = sqrt(2(h2 - h1))
   B. C2 = sqrt(2(h1 - h2) + C1^2)
   C. C2 = 2(h1 - h2)
   D. C2 = sqrt(h1 - h2)
   Answer: B. From h1 + C1^2/2 = h2 + C2^2/2, C2 = sqrt(2(h1 - h2) + C1^2) = sqrt(2(h01 - h2)). (Key point: Exit velocity from energy equation)

2. Nozzle efficiency is
   A. actual mass flow / ideal mass flow
   B. actual exit pressure / inlet pressure
   C. isentropic temperature drop / actual drop
   D. actual kinetic energy gain / isentropic kinetic energy gain between the same pressures
   Answer: D. eta_n = (h01 - h2)/(h01 - h2s) = C2^2/C2s^2 for the same pressure ratio. (Key point: Nozzle efficiency definition)

3. How is the velocity coefficient related to nozzle efficiency?
   A. Cv = sqrt(eta_n)
   B. Cv = eta_n
   C. Cv = eta_n^2
   D. Cv = 1 - eta_n
   Answer: A. Cv = C2/C2s and eta_n = C2^2/C2s^2, so Cv = sqrt(eta_n); Cv of 0.95 to 0.99 gives eta_n about 0.90 to 0.98. (Key point: Velocity coefficient)

4. On the T-s diagram, where does the actual exit state 2 lie relative to the isentropic state 2s?
   A. At a lower temperature than 2s
   B. At the same state as 2s
   C. At a higher temperature (enthalpy) than 2s because friction heats the gas
   D. At a higher pressure than 2s
   Answer: C. Friction adds entropy, so h2 > h2s and less kinetic energy is produced. (Key point: Loss on T-s diagram)

5. Which statement about the actual nozzle process is correct?
   A. Total temperature falls and total pressure is unchanged
   B. Total temperature is unchanged but total pressure falls, p02 < p01
   C. Both totals are unchanged
   D. Cd is the ratio of actual to ideal exit velocity
   Answer: B. The process is adiabatic so T0 is constant, but losses reduce p0. Cd is the ratio of actual to ideal mass flow. (Key point: Discharge coefficient and total pressure)

## Related in Turbo Machines

- [Gas turbine nozzle: principle and types](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Anozzle-principle-types) — Turbo Machines, chapter 4
- [Convergent-divergent nozzle with efficiency](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Acd-nozzle-efficiency-exit-area-numerical) — Turbo Machines, chapter 4
- [Impulse turbine blade work and diagram efficiency](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Aimpulse-turbine-diagram-efficiency) — Turbo Machines, chapter 2
- [Gas turbine power from isentropic efficiency](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Agas-turbine-power-isentropic-efficiency) — Turbo Machines, chapter 1
- [Axial gas turbine stage design calculation](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Aaxial-turbine-stage-gas-numerical) — Turbo Machines, chapter 2
- [Convergent nozzle: choking and mass flow](https://www.bctengineer.com/question.md?key=semester_7%2Fturbo_machines%3Aconvergent-nozzle-choking-mass-flow) — Turbo Machines, chapter 4

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- [Velocity, head loss, discharge in loop pipes BC, CD, BF, FD](https://www.bctengineer.com/question.md?key=semester_5%2Fwater_supply_engineering%3Aloop-a76) — Water Supply Engineering, chapter 7
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