12.4 Impulse-Momentum Equation and Forces on Control Volumes

Key Takeaways

  • NCEES lists energy, impulse, and momentum equations as one Fluid Mechanics sub-topic, so the momentum equation is examinable alongside Bernoulli's equation.
  • The steady-flow momentum equation states that the sum of external forces equals mass flow rate times the change in velocity, applied separately in each direction.
  • Momentum is a vector equation, so a pipe bend generates a reaction force even when the speed is unchanged, because the direction changed.
  • The momentum equation applies even when energy is dissipated, which is why it works across a sudden expansion or a hydraulic jump where Bernoulli's equation fails.
  • A jet striking a stationary flat plate normally exerts a force of rho Q V, and a 180-degree deflection doubles that force.
Last updated: August 2026

12.4 Impulse-Momentum Equation and Forces on Control Volumes

The NCEES sub-topic is "Energy, impulse, and momentum equations (e.g., Bernoulli equation)." The energy half is covered in the continuity and Bernoulli section; this section covers the momentum half, which answers a different question: not how fast the fluid moves, but what force it exerts on the hardware. Anchor blocks, thrust blocks, nozzle reactions, and turbine blade forces are all momentum problems.

The Steady-Flow Momentum Equation

F=m˙(VoutVin),m˙=ρQ=ρAV\sum \vec{F} = \dot{m}\left(\vec{V}_{\text{out}} - \vec{V}_{\text{in}}\right), \qquad \dot{m} = \rho Q = \rho A V

Applied component by component:

Fx=m˙(V2xV1x),Fy=m˙(V2yV1y)\sum F_x = \dot{m}(V_{2x} - V_{1x}), \qquad \sum F_y = \dot{m}(V_{2y} - V_{1y})

The forces on the left side include every external force on the control volume:

ForceExpressionNote
Pressure at inlet$+p_1A_1$Acts into the control volume, along the inlet flow direction
Pressure at outlet$-p_2A_2$Acts into the control volume, against the outlet flow direction
Reaction from the structure$R_x, R_y$Usually the unknown you are solving for
Weight of contained fluid$-W$Often neglected for short fittings

Use gauge pressures. Atmospheric pressure acts uniformly on the outside of the fitting and cancels, so working in gauge pressure automatically accounts for it. Mixing absolute and gauge is a reliable way to get a wrong anchor force.

Why Momentum Succeeds Where Bernoulli Fails

Bernoulli / energy equationMomentum equation
NatureScalarVector
Valid with energy loss?No (unless a loss term is added)Yes, always
Gives youPressures and velocitiesForces
Needs internal detail?Yes, to quantify lossesNo — only inlet and outlet conditions

This is the key insight of the topic. Across a sudden expansion, a hydraulic jump, or a partly closed valve, the internal flow is violently turbulent and energy is destroyed in ways you cannot compute from geometry. Bernoulli's equation is invalid there. The momentum equation does not care: it needs only what crosses the control surface, so it works across the most dissipative device imaginable. When a question asks for a force across a lossy transition, momentum is the only usable tool.

Forces on Pipe Bends

For a bend turning flow through angle $\theta$ in the horizontal plane, with the inlet along $+x$:

Rx=m˙(V2cosθV1)p1A1+p2A2cosθR_x = \dot{m}(V_2\cos\theta - V_1) - p_1A_1 + p_2A_2\cos\theta Ry=m˙(V2sinθ0)+p2A2sinθR_y = \dot{m}(V_2\sin\theta - 0) + p_2A_2\sin\theta

A bend generates force even at constant speed. In a constant-diameter bend $V_1 = V_2$ in magnitude, so nothing changes energetically — yet the momentum vector rotates, and that requires a force. This is why a 90° elbow in a large water main needs a thrust block even though the pressure and velocity are the same on both sides.

Worked Example: Anchor Force on a 90° Reducing Bend

A horizontal 90° bend reduces from $D_1 = 300$ mm to $D_2 = 200$ mm. Water ($\rho = 1{,}000$ kg/m³) flows at $Q = 0.15$ m³/s. Inlet gauge pressure is 250 kPa; outlet gauge pressure is 220 kPa. Inlet flow is along $+x$, outlet along $+y$. Find the anchoring force.

Areas and velocities:

A1=π(0.300)24=0.07069 m2,V1=0.150.07069=2.122 m/sA_1 = \frac{\pi(0.300)^2}{4} = 0.07069\ \text{m}^2, \qquad V_1 = \frac{0.15}{0.07069} = 2.122\ \text{m/s} A2=π(0.200)24=0.03142 m2,V2=0.150.03142=4.775 m/sA_2 = \frac{\pi(0.200)^2}{4} = 0.03142\ \text{m}^2, \qquad V_2 = \frac{0.15}{0.03142} = 4.775\ \text{m/s} m˙=ρQ=1,000(0.15)=150 kg/s\dot{m} = \rho Q = 1{,}000(0.15) = 150\ \text{kg/s}

$x$ direction (outlet has no $x$ velocity, and $\theta = 90°$ so $\cos\theta = 0$):

Rx+p1A1=m˙(0V1)R_x + p_1A_1 = \dot{m}(0 - V_1) Rx=m˙V1p1A1=150(2.122)250,000(0.07069)R_x = -\dot{m}V_1 - p_1A_1 = -150(2.122) - 250{,}000(0.07069) Rx=318.317,672=17,990 NR_x = -318.3 - 17{,}672 = -17{,}990\ \text{N}

$y$ direction (inlet has no $y$ velocity):

Ryp2A2=m˙(V20)R_y - p_2A_2 = \dot{m}(V_2 - 0) Ry=m˙V2+p2A2=150(4.775)+220,000(0.03142)R_y = \dot{m}V_2 + p_2A_2 = 150(4.775) + 220{,}000(0.03142) Ry=716.3+6,912=7,628 NR_y = 716.3 + 6{,}912 = 7{,}628\ \text{N}

Resultant:

R=(17,990)2+(7,628)2=3.236×108+5.819×107=3.818×108=19,540 N19.5 kNR = \sqrt{(17{,}990)^2 + (7{,}628)^2} = \sqrt{3.236\times10^8 + 5.819\times10^7} = \sqrt{3.818\times10^8} = \boxed{19{,}540\ \text{N} \approx 19.5\ \text{kN}}

ϕ=arctan ⁣(7,62817,990)=23.0° from the x axis\phi = \arctan\!\left(\frac{7{,}628}{17{,}990}\right) = 23.0° \text{ from the } -x \text{ axis}

Note the dominance of the pressure terms. The momentum flux contributions are only 318 N and 716 N, while the pressure-area terms are 17{,}672 N and 6{,}912 N — over 20 times larger. For pressurized liquid systems, the anchor force is essentially a pressure-times-area problem, and neglecting the momentum flux entirely would introduce under 5% error. The reverse is true for high-velocity, low-pressure jets, where momentum flux dominates. Recognizing which regime you are in is a fast sanity check on the magnitude of your answer.

Jets Striking Surfaces

For a jet of area $A$ and velocity $V$, with $\dot{m} = \rho A V = \rho Q$:

TargetForce on the target
Stationary flat plate, normal to jet$F = \rho Q V = \rho A V^2$
Stationary plate inclined at $\theta$ to the jet$F_{\text{normal}} = \rho Q V\sin\theta$
Stationary curved vane, 180° reversal$F = 2\rho Q V$
Curved vane deflecting through $\theta$$F_x = \rho Q V(1-\cos\theta)$
Plate moving away at $u$$F = \rho A(V-u)^2$
Series of vanes (turbine wheel) moving at $u$$F = \rho A V(V-u)$

The 180° result is worth remembering: reversing a jet gives twice the force of stopping it, because the momentum change is from $+V$ to $-V$, a total of $2V$. This is the principle of the Pelton turbine bucket, and it is why the buckets are split to turn the jet nearly back on itself.

Worked Example: Jet on a Moving Vane and Maximum Power

A 40 mm diameter water jet at 30 m/s strikes a single vane that deflects it 180° and moves away at 12 m/s. Find the force and power, then the velocity that maximizes power.

A=π(0.040)24=1.257×103 m2A = \frac{\pi(0.040)^2}{4} = 1.257\times10^{-3}\ \text{m}^2

Relative velocity governs the interaction: $V_{\text{rel}} = 30 - 12 = 18$ m/s.

F=2ρA(Vu)2=2(1,000)(1.257×103)(18)2=2(1,000)(1.257×103)(324)=814.6 NF = 2\rho A(V-u)^2 = 2(1{,}000)(1.257\times10^{-3})(18)^2 = 2(1{,}000)(1.257\times10^{-3})(324) = 814.6\ \text{N}

P=Fu=814.6(12)=9,775 W=9.78 kWP = Fu = 814.6(12) = 9{,}775\ \text{W} = \boxed{9.78\ \text{kW}}

Maximizing power. With $P = 2\rho A(V-u)^2u$, differentiate with respect to $u$:

dPdu=2ρA[(Vu)22u(Vu)]=2ρA(Vu)[(Vu)2u]=0\frac{dP}{du} = 2\rho A\left[(V-u)^2 - 2u(V-u)\right] = 2\rho A(V-u)\left[(V-u) - 2u\right] = 0

V3u=0    u=V3=10 m/sV - 3u = 0 \;\Rightarrow\; u = \frac{V}{3} = 10\ \text{m/s}

Pmax=2(1,000)(1.257×103)(3010)2(10)=2(1,000)(1.257×103)(400)(10)=10,056 W=10.06 kWP_{\max} = 2(1{,}000)(1.257\times10^{-3})(30-10)^2(10) = 2(1{,}000)(1.257\times10^{-3})(400)(10) = 10{,}056\ \text{W} = 10.06\ \text{kW}

So $u = V/3$ for a single vane, giving 10.06 kW versus 9.78 kW at 12 m/s — only 3% better, showing the optimum is quite flat.

A caution the exam exploits: for a series of vanes on a turbine wheel, where the jet is continuously intercepted, the force is $\rho AV(V-u)$ rather than $\rho A(V-u)^2$, and the optimum shifts to $u = V/2$ with 50% theoretical efficiency for a flat vane. The $V/2$ result is the one usually quoted for Pelton wheels. Read whether the problem describes one vane or a wheel.

Test Your Knowledge

A 90-degree elbow of constant diameter carries water at constant speed. Is a thrust force generated?

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Test Your Knowledge

A water jet delivering 0.020 m^3/s at 25 m/s strikes a stationary vane that reverses it through 180 degrees. What force does the jet exert on the vane?

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Test Your Knowledge

Why can the momentum equation be applied across a sudden pipe expansion where Bernoulli's equation cannot?

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Test Your Knowledge

For a single vane moving away from a jet and reversing it through 180 degrees, what vane speed maximizes the extracted power?

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