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Gradual valve closure with retardation law

Short answer

With gradual closure and retardation proportional to t^(5/4), rigid-column analysis gives velocity 1.52 m/s and valve inlet head 415 m at t=6 s.

A valve which normally operates under a net head of 300 m is supplied with water at 2.5 m³/s through a pipe 1 m diameter and 1.6 km long for which f = 0.02. When the valve is gradually stopped over an interval of 8 seconds, the retardation of the water being proportional to t5/4t^{5/4}, i.e. a∝t5/4a \propto t^{5/4}, where t represents the time measured from the beginning of the shut-down. Neglecting minor losses and assuming an incompressible fluid in a rigid pipe with f independent of Reynolds number, determine the head at the valve inlet and the velocity in the pipe at t = 6 seconds.

Data. Normal net head at the valve =300= 300 m with Q=2.5Q = 2.5 m³/s; D=1D = 1 m, L=1.6L = 1.6 km, f=0.02f = 0.02; the valve is closed gradually over T=8T = 8 s with retardation a∝t5/4a \propto t^{5/4}. The pipe is treated as rigid and the water as incompressible (rigid-column theory); minor losses are neglected.

Initial velocity and reservoir head

V0=QπD2/4=3.183 m/s,hf0=fLDV022g=0.02(1600)3.183219.62=16.53 mV_0 = \frac{Q}{\pi D^2/4} = 3.183\ \text{m/s},\qquad h_{f0} = f\frac{L}{D}\frac{V_0^2}{2g} = 0.02(1600)\frac{3.183^2}{19.62} = 16.53\ \text{m}

The head at the upstream end of the pipe (reservoir level) is the valve head plus the friction loss: HR=300+16.53=316.53H_R = 300 + 16.53 = 316.53 m.

Velocity during closure

a=kt5/4a = kt^{5/4}, and the velocity falls to zero at t=Tt = T: V0=∫0Tkt5/4 dt=49kT9/4\displaystyle V_0 = \int_0^T kt^{5/4}\,dt = \frac{4}{9}kT^{9/4}, so k=9V04T9/4k = \dfrac{9V_0}{4T^{9/4}}. Then

V(t)=V0−∫0ta dt=V0[1−(tT)9/4]V(t) = V_0 - \int_0^t a\,dt = V_0\left[1 - \left(\frac{t}{T}\right)^{9/4}\right]

At t=6t = 6 s: (68)2.25=0.5235\left(\dfrac{6}{8}\right)^{2.25} = 0.5235, so

V=3.183(1−0.5235)=1.517 m/sV = 3.183(1 - 0.5235) = 1.517\ \text{m/s}

Head at the valve at t=6t = 6 s

Retardation a=∣dVdt∣=94V0t5/4T9/4=2.25(3.183)61.2582.25=0.6248 m/s2a = \left|\dfrac{dV}{dt}\right| = \dfrac{9}{4}V_0\dfrac{t^{5/4}}{T^{9/4}} = 2.25(3.183)\dfrac{6^{1.25}}{8^{2.25}} = 0.6248\ \text{m/s}^2.

Equation of motion of the water column (deceleration raises the head at the valve):

Hvalve=HR−fLDV22g+LgaH_{valve} = H_R - f\frac{L}{D}\frac{V^2}{2g} + \frac{L}{g}a Hvalve=316.53−3.75+1600(0.6248)9.81=316.53−3.75+101.91=414.7 mH_{valve} = 316.53 - 3.75 + \frac{1600(0.6248)}{9.81} = 316.53 - 3.75 + 101.91 = 414.7\ \text{m}

Answer: At t=6t = 6 s, the velocity in the pipe is 1.521.52 m/s and the head at the valve is about 415415 m. This is about 115 m above the normal 300 m: 101.9 m comes from the deceleration, and 12.8 m because the friction loss has dropped from 16.53 m to 3.75 m.

✓ Answer checked by Claude Opus 5.5 (high effort)

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