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Convergent nozzle: choking and mass flow

Short answer

Critical pressure p* = 264.1 kPa. (a) At 350 kPa back pressure the nozzle is unchoked: exit pressure 350 kPa, exit velocity 312.0 m/s, mass flow 1.685 kg/s. (b) At 200 kPa the nozzle is choked: exit pressure 264.1 kPa, exit velocity 409.2 m/s, mass flow 1.808 kg/s.

Air at a stagnation pressure of 500 kPa and a stagnation temperature of 500 K flows isentropically through a convergent nozzle of exit area 20 cm². Find the exit velocity, exit pressure and mass flow rate when the back pressure is (a) 350 kPa and (b) 200 kPa. Take γ=1.4\gamma = 1.4, R=0.287R = 0.287 kJ/kg K.

Critical pressure ratio for air:

p∗p0=(2γ+1)γ/(γ−1)=0.5283  ⇒  p∗=0.5283×500=264.1 kPa\frac{p^*}{p_0} = \left(\frac{2}{\gamma + 1}\right)^{\gamma/(\gamma-1)} = 0.5283 \;\Rightarrow\; p^* = 0.5283 \times 500 = 264.1\ \text{kPa}

(a) Back pressure 350 kPa

Since 350>264.1350 > 264.1 kPa, the nozzle is not choked and the exit pressure equals the back pressure, pe=350p_e = 350 kPa.

Te=T0(pep0)0.2857=500×0.70.2857=451.6 KT_e = T_0\left(\frac{p_e}{p_0}\right)^{0.2857} = 500 \times 0.7^{0.2857} = 451.6\ \text{K} Ce=2cp(T0−Te)=2×1005×48.4=312.0 m/sC_e = \sqrt{2c_p(T_0 - T_e)} = \sqrt{2 \times 1005 \times 48.4} = 312.0\ \text{m/s} ρe=peRTe=3500.287×451.6=2.701 kg/m3\rho_e = \frac{p_e}{RT_e} = \frac{350}{0.287 \times 451.6} = 2.701\ \text{kg/m}^3 m˙=ρeCeAe=2.701×312.0×0.0020=1.685 kg/s\dot m = \rho_e C_e A_e = 2.701 \times 312.0 \times 0.0020 = 1.685\ \text{kg/s}

Exit Mach number =312.0/1.4×287×451.6=0.73= 312.0/\sqrt{1.4 \times 287 \times 451.6} = 0.73.

(b) Back pressure 200 kPa

Since 200<264.1200 < 264.1 kPa, the nozzle is choked. The exit pressure is p∗=264.1p^* = 264.1 kPa (the remaining drop to 200 kPa takes place outside the nozzle) and Mae=1Ma_e = 1.

T∗=2T0γ+1=2×5002.4=416.7 KT^* = \frac{2T_0}{\gamma + 1} = \frac{2 \times 500}{2.4} = 416.7\ \text{K} C∗=γRT∗=1.4×287×416.7=409.2 m/sC^* = \sqrt{\gamma R T^*} = \sqrt{1.4 \times 287 \times 416.7} = 409.2\ \text{m/s} ρ∗=p∗RT∗=264.10.287×416.7=2.209 kg/m3\rho^* = \frac{p^*}{RT^*} = \frac{264.1}{0.287 \times 416.7} = 2.209\ \text{kg/m}^3 m˙max=ρ∗C∗A=2.209×409.2×0.0020=1.808 kg/s\dot m_{max} = \rho^* C^* A = 2.209 \times 409.2 \times 0.0020 = 1.808\ \text{kg/s}

Lowering the back pressure further does not change the mass flow; it can only be raised by increasing p0p_0 or AA.

Casepep_e (kPa)CeC_e (m/s)m˙\dot m (kg/s)
(a) 350 kPa350312.01.685
(b) 200 kPa (choked)264.1409.21.808

Answer: (a) CeC_e = 312.0 m/s, m˙\dot m = 1.685 kg/s; (b) choked, pep_e = 264.1 kPa, CeC_e = 409.2 m/s, m˙\dot m = 1.808 kg/s.

✓ Answer checked by Claude Opus 5.5 (high effort)

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