Engineering
Centrifugal pump
Run a centrifugal pump into a pipe that lifts water ten metres: the flow settles where the pump curve H = K1 w^2 - K2 w Q - K3 Q|Q| crosses the system curve Hs + R Q|Q|, exactly the closed-form root. Throttle the discharge valve and watch the point climb the pump curve at less flow and more head; slow the motor and compare with the affinity laws, which hold only when the static head is taken away; drop below the speed whose shutoff head equals the lift and the flow stops. The motor’s work is booked against the lift, the pipe and internal losses, the disk friction and the kinetic energy of wheel and water.

What happens
A motor ramps a centrifugal pump to its set speed; the water in a 50 m pipe of 0.01 m² accelerates by dQ/dt = (g·A/L)·(H − H_sys) until the pump’s head K_1·ω² − K_2·ω·Q − K_3·Q|Q| meets the static lift plus the pipe and valve losses, the closed-form root of the two curves. The hydraulic torque is ρ·g·Q·(K_1·ω − K_2·Q), disk friction and a constant torque are the shaft losses, and the valve’s resistance grows as 1/opening². Each millisecond books the motor’s work against the lift, the losses and the kinetic energy of wheel and water, so the ledger closes to rounding; without static head the operating points at two speeds are homologous and the affinity laws hold exactly.
Try this
Let the flow settle and compare it with the closed-form crossing; throttle the valve and read the head climb; slow the motor with and without static head and check the affinity laws.
The model and its limits
A quadratic pump curve and a quadratic system curve, a rigid water column in a straight pipe, no cavitation or NPSH, a drive that holds its set speed. Not a selection of a real pump.
Equations used in the module
Equations H = K_1·ω² − K_2·ω·Q − K_3·Q·|Q|, H_sys = H_s + (R_p + R_v/x²)·Q·|Q| dQ/dt = (g·A/L)·(H − H_sys), T_h = ρ·g·Q·(K_1·ω − K_2·Q) Q_2/Q_1 = ω_2/ω_1, H_2/H_1 = (ω_2/ω_1)² (H_s = 0) W_motor = E_k + ρ·g·H_s·V + Q_pipe + Q_int + Q_fr


