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Specific force and venturi flume relations

Short answer

Specific force is F = Q^2/(gA) + Aȳ (momentum function). For given F, Q is max at critical state because dQ/dy=0 yields Fr=1. Applying this to a venturi flume with critical flow at the throat gives Q = 3.13 b H^(3/2)(h/H)^(3/2) and b/B = (H/h)√(3 − 2 H/h).

What is specific force? Prove that for a given specific force the discharge in a given channel section is maximum when the flow is in the critical state. A venturiflume in a rectangular channel of width B has the throat width of b. The depth of liquid at entry is H and at the throat is h. Prove that following relation exists for the discharge and width ratio: Q=3.13 bH3/2(hH)3/2Q = 3.13\,bH^{3/2}\left(\frac{h}{H}\right)^{3/2} and bB=3(hH)−3(hH)3/2\frac{b}{B} = \sqrt{3}\left(\frac{h}{H}\right) - \sqrt{3}\left(\frac{h}{H}\right)^{3/2}.

Specific force

The specific force (momentum function) is the sum of the momentum flux and the hydrostatic pressure force per unit weight of water at a section:

F=Q2gA+AyˉF = \frac{Q^2}{gA} + A\bar{y}

where AA is the flow area and yˉ\bar y is the depth of the centroid below the free surface. For a given QQ, FF is minimum at the critical depth, and the two depths with equal FF are the conjugate depths of a hydraulic jump.

Discharge is maximum at critical state for a given FF

From the definition, Q2=gA (F−Ayˉ)Q^2 = gA\,(F - A\bar y). For fixed FF and a given section, QQ is a function of yy only. For QQ to be a maximum, dQ2/dy=0dQ^2/dy = 0:

ddy(AF−A2yˉ)=0\frac{d}{dy}\left(AF - A^2\bar y\right) = 0

Use dA/dy=TdA/dy = T (top width) and d(Ayˉ)/dy=Ad(A\bar y)/dy = A (the first moment of area increases by A dyA\,dy when the depth increases by dydy):

TF−[A⋅A+Ayˉ⋅T]=0T (F−Ayˉ)=A2\begin{aligned} TF - \left[A\cdot A + A\bar y\cdot T\right] &= 0 \\ T\,(F - A\bar y) &= A^2 \end{aligned}

Now F−Ayˉ=Q2/(gA)F - A\bar y = Q^2/(gA), so

Q2TgA=A2  ⇒  Q2TgA3=1\frac{Q^2 T}{gA} = A^2 \;\Rightarrow\; \frac{Q^2 T}{gA^3} = 1

This is exactly the condition Fr=1Fr = 1 for critical flow. The second derivative is negative, so this is a maximum. Hence for a given specific force the discharge is maximum at the critical state.

Venturi flume: discharge

Assume the flow passes through critical depth at the throat, so h=ych = y_c. For a rectangular throat of width bb:

Q=b g h3/2=9.81 b h3/2=3.13 b h3/2Q = b\,\sqrt{g}\,h^{3/2} = \sqrt{9.81}\,b\,h^{3/2} = 3.13\,b\,h^{3/2}

Writing h3/2=H3/2(hH)3/2h^{3/2} = H^{3/2}\left(\dfrac{h}{H}\right)^{3/2}:

Q=3.13 b H3/2(hH)3/2Q = 3.13\,b\,H^{3/2}\left(\frac{h}{H}\right)^{3/2}

Venturi flume: width ratio

Apply the energy equation between the entry (depth HH, width BB) and the throat (critical, E=32hE = \tfrac{3}{2}h), neglecting losses and with a level bed:

H+Q22gB2H2=32hH + \frac{Q^2}{2gB^2H^2} = \frac{3}{2}h

Put Q2=g b2h3Q^2 = g\,b^2h^3 (critical flow at the throat):

H+b2h32B2H2=32h  ⇒  b2B2=2H2h3(32h−H)=3(Hh)2−2(Hh)3H + \frac{b^2h^3}{2B^2H^2} = \frac{3}{2}h \;\Rightarrow\; \frac{b^2}{B^2} = \frac{2H^2}{h^3}\left(\frac{3}{2}h - H\right) = 3\left(\frac{H}{h}\right)^2 - 2\left(\frac{H}{h}\right)^3 bB=Hh3−2Hh\boxed{\frac{b}{B} = \frac{H}{h}\sqrt{3 - 2\frac{H}{h}}}

Check: with H=1 mH = 1\ \text{m}, h=0.8 mh = 0.8\ \text{m} this gives b/B=0.884b/B = 0.884. For B=3 mB = 3\ \text{m}, b=2.652 mb = 2.652\ \text{m}, Q=3.13×2.652×0.81.5=5.94 m3/sQ = 3.13 \times 2.652 \times 0.8^{1.5} = 5.94\ \text{m}^3/\text{s}, and the energy at entry =1+0.2=1.2=1.5×0.8= 1 + 0.2 = 1.2 = 1.5 \times 0.8. This agrees.

Note: the second form printed in the question, 3 (h/H)−3 (h/H)3/2\sqrt3\,(h/H) - \sqrt3\,(h/H)^{3/2}, does not reduce to b/B=1b/B = 1 when there is no contraction, so the standard energy-equation result above is used. The discharge relation is exactly as given.

✓ Answer checked by Claude Opus 5.5 (high effort)

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