Unsteady Tank Draining – Time to Lower Level from H1 to H2 A tank of uniform cross-sectional area A with a small orifice of area a at the bottom drains under gravity. The time required to drop the liquid level from H1 to H2 (including discharge coefficient Cd) is t = (2 * A / (Cd * a * sqrt(2 * g))) * (sqrt(H1) − sqrt(H2)).
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At = (2 * A / (Cd * a * sqrt(2 * g))) * (sqrt(H1) − sqrt(H2))
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Bt = (A / (Cd * a)) * (H1 − H2)
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Ct = (A / (Cd^2 * a^2 * g)) * ln(H1 / H2)
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Dt = (2 * A / (a * sqrt(2 * g))) * (H1 − H2)
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Et = (A / (Cd * a * sqrt(g))) * (sqrt(H1) + sqrt(H2))
Answer
Correct Answer: t = (2 * A / (Cd * a * sqrt(2 * g))) * (sqrt(H1) − sqrt(H2))
Explanation
Introduction:Predicting drain-down time is a classic unsteady-flow problem. The solution uses Bernoulli’s principle with Torricelli’s efflux velocity and the continuity equation for a falling head in a reservoir-orifice configuration.
Given Data / Assumptions:
- Tank cross-section A; small orifice area a at bottom.
- Coefficient of discharge Cd accounts for contraction and velocity effects.
- Inviscid energy assumptions aside from Cd; negligible velocity of the tank free surface.
Concept / Approach:
Torricelli’s result gives exit speed V = Cd * sqrt(2 * g * H), so discharge Q = a * V = Cd * a * sqrt(2 * g * H). The falling head yields A * dH/dt = −Q. Separating variables produces an integral in 1/sqrt(H).
Step-by-Step Solution:
1) Write A * dH/dt = −Cd * a * sqrt(2 * g * H).2) Rearrange: dH / sqrt(H) = −(Cd * a * sqrt(2 * g) / A) * dt.3) Integrate H from H1 to H2 and t from 0 to t.4) Use ∫ dH / sqrt(H) = 2 (sqrt(H2) − sqrt(H1)).5) Solve for t to get t = (2 * A / (Cd * a * sqrt(2 * g))) * (sqrt(H1) − sqrt(H2)).Verification / Alternative check:
Setting H2 = 0 gives complete emptying time, matching standard textbook expressions. Dimensional check confirms seconds for t.
Why Other Options Are Wrong:
Linear dependence on H (Option B, D) contradicts the square-root head relation. Logarithmic form (Option C) suits viscous laminar draining in tubes, not orifices. Option E has incorrect dependence on H and g.
Common Pitfalls:
Forgetting Cd; using A ≈ constant assumption where it is invalid (e.g., conical tanks); neglecting approach velocity corrections for large a/A.
Final Answer:
t = (2 * A / (Cd * a * sqrt(2 * g))) * (sqrt(H1) − sqrt(H2))