Momentum Control Volumes and Turbomachinery
Key Takeaways
- Use the linear momentum equation ΣF = ṁ(V_out − V_in) when a problem asks for force from a change in flow direction or speed.
- Momentum is vector-based, so x and y components must be written separately before combining into a resultant.
- Pressure forces belong on the control surface unless the flow exits to atmosphere, where gauge pressure is zero at that boundary.
- Mass flow rate is ṁ = ρQ = ρAV; using volume flow rate directly in momentum equations is a frequent FE error.
- Turbomachinery questions use head, flow rate, speed, efficiency, and the affinity laws rather than detailed blade design.
- Specific speed N_s groups speed, flow, and head to classify pumps as radial, mixed, or axial flow.
The Linear Momentum Equation
The FE tests a clean division of labor: use the energy equation for heads, velocities, and power, but use the momentum equation whenever a question asks for a force — the reaction on a pipe bend, the thrust of a jet, the force on a deflecting vane, the anchor force on a nozzle. For steady flow through a control volume:
ΣF = ṁ(V_out − V_in) = ṁ ΔV
where ṁ = ρQ = ρAV is the mass flow rate. The sum of forces on the control volume includes pressure forces on the inlet/outlet faces (p·A acting inward on each face), the support/anchor reaction, and gravity/weight if relevant. Because momentum is a vector, you must split into components and solve each axis independently:
- ΣF_x = ṁ(V_2x − V_1x)
- ΣF_y = ṁ(V_2y − V_1y)
Set a consistent sign convention (e.g., right and up positive), track the signed velocity components, then combine: F_R = √(F_x² + F_y²) with direction θ = arctan(F_y/F_x). The single most common error is using volume flow Q where ṁ = ρQ is required; the second is dropping the inlet pressure force when inlet pressure is gauge-nonzero.
Worked Example — Reducing Elbow
Water (ρ = 1000 kg/m³) flows through a 90° elbow. Inlet: V₁ = 4 m/s, A₁ = 0.02 m², gauge pressure p₁ = 200 kPa, flow in +x. Outlet: discharges to atmosphere (p₂ = 0 gauge) in +y, with V₂ = 8 m/s (smaller exit area).
Mass flow: ṁ = ρA₁V₁ = 1000 × 0.02 × 4 = 80 kg/s.
x-momentum: p₁A₁ + R_x = ṁ(0 − V₁). p₁A₁ = 200,000 × 0.02 = 4000 N. So R_x = ṁ(−V₁) − p₁A₁ = 80(−4) − 4000 = −4320 N (the support pushes in −x).
y-momentum: R_y = ṁ(V₂ − 0) = 80 × 8 = 640 N.
Resultant anchor force: F_R = √(4320² + 640²) ≈ 4367 N. Note the pressure term dominates here — never drop it when inlet pressure is gauge-nonzero.
Jets, Vanes, and Thrust
A free jet striking a stationary flat plate normal to the flow exerts F = ṁV = ρAV². For a jet turned through angle θ by a vane, the force components follow directly from the inlet/outlet velocity components. A jet reversed 180° by a curved vane delivers F = ṁ(V − (−V)) = 2ṁV — twice the force of a flat plate, a classic FE distinction.
For a moving vane (turbine blade), the relative velocity (V − u) replaces V, where u is the blade speed, and the effective mass flow is ρA(V − u). Power extracted = F × u, and it is maximized when u = V/2 for a single moving plate.
Rocket/jet thrust: Thrust = ṁ_exit V_exit + (p_exit − p_atm)A_exit. The momentum-flux term ṁV usually dominates; the pressure term matters only for under- or over-expanded nozzles.
Worked example — flat plate. A 25 mm-diameter water jet at 15 m/s hits a stationary plate normal to flow. A = π(0.025)²/4 = 4.91 × 10⁻⁴ m². ṁ = ρAV = 1000 × 4.91e-4 × 15 = 7.36 kg/s. F = ṁV = 7.36 × 15 = 110 N.
| Target | Deflection | Force on target |
|---|---|---|
| Flat plate ⊥ stationary jet | 90° | ṁV = ρAV² |
| Vane turning jet 90° | 90° | ṁV per axis |
| Vane reversing jet 180° | 180° | 2ṁV |
| Moving plate (speed u) | 90° | ρA(V−u)² |
Turbomachinery and the Affinity Laws
For pumps, fans, and turbines, the FE rarely asks blade geometry — it asks head, flow, power, efficiency, and scaling. The affinity laws relate performance of a single pump at different speeds N (or geometrically similar pumps at diameter ratio D):
- Flow: Q₂/Q₁ = (N₂/N₁) — flow scales linearly with speed.
- Head: h₂/h₁ = (N₂/N₁)² — head scales with speed squared.
- Power: P₂/P₁ = (N₂/N₁)³ — power scales with speed cubed.
Worked example. A pump runs at 1750 rpm delivering Q = 0.10 m³/s, h = 25 m, P = 30 kW. Sped up to 2100 rpm (ratio 1.2): Q = 0.10 × 1.2 = 0.12 m³/s; h = 25 × 1.2² = 36 m; P = 30 × 1.2³ = 51.8 kW.
Specific speed N_s = N√Q/h^(3/4) classifies the impeller type independent of size. Low N_s indicates radial (centrifugal, high-head, low-flow) pumps; mid N_s indicates mixed-flow; high N_s indicates axial (propeller, low-head, high-flow) pumps. It tells a designer which geometry suits a given duty.
Worked example — turbine power. Water (Q = 0.5 m³/s) drops through a net head of 60 m to a turbine with overall efficiency 0.85. Available hydraulic power = γQh = 9810 × 0.5 × 60 = 294 kW. Shaft power out = 294 × 0.85 = 250 kW. Note efficiency reduces output for a turbine but increases required input for a pump — the direction flips with the device.
Sign convention: a pump/fan adds head and power to the fluid (h_p positive in the energy equation); a turbine extracts it (h_t positive on the downstream side). Confusing the direction flips the entire energy balance and the efficiency placement.
A water jet (ρ = 1000 kg/m³) of area 0.001 m² and velocity 20 m/s strikes a stationary flat plate normal to the jet. The force on the plate is:
A pump's speed is increased by a factor of 1.5. By the affinity laws, the power requirement changes by a factor of approximately:
In the momentum equation ΣF = ṁ(V_out − V_in), what does ṁ equal?
A pump operating at 1200 rpm delivers 30 m of head. If the speed is reduced to 600 rpm, the head delivered (affinity laws) becomes approximately: