The Equation of Continuity — Question 6

Section 14-8 · Physics pages 2202–2203

Question 6 A conical tank rises quickly near its tip An open conical tank has its vertex downward, total height H and top radius R. It is filled at constant volume rate Q from a level h1 > 0 to h2. There is no outflow, and the liquid is incompressible. h Conical tank cross section; the horizontal line marks the current liquid level. (a) Derive dh/dt in terms of current height h and derive the filling time from h1 to h2. (b) Evaluate the time for H = 1.0 m, R = 0.50 m, Q = 1.0 × 10−3 m3/s, h1 = 0.20 m and h2 = 0.60 m. Explain the formal behavior as h →0.
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Question 6 - Solution A conical tank rises quickly near its tip h (a) Derivation and calculation Similar triangles give r(h) = Rh/H, hence A(h) = πR2h2/H2, Q = dV dt = A(h)dh dt . dh dt = QH2 πR2h2 . ∆t = πR2 QH2 ∫h2 h1 h2 dh = πR2(h3 2 −h3 1) 3QH2 . (b) Result and interpretation ∆t = π(.500)2(.6003 −.2003) 3(.00100)(1.00)2 = 54.4543 s . h →0+ : A(h) →0, dh/dt →∞, Q = finite. The divergence concerns height rate, not incoming volume rate; finite inlet geometry and wetting limit the tip idealization. Physical check The same time follows from [V (h2) −V (h1)]/Q with V (h) = πR2h3/(3H2).

Question 6

A conical tank rises quickly near its tip

An open conical tank has its vertex downward, total height HH and top radius RR. It is filled at constant volume rate QQ from a level h1>0h_1>0 to h2h_2. There is no outflow, and the liquid is incompressible.

Diagram shown in the original SVG worksheet.

  1. Derive dh/dtdh/dt in terms of current height hh and derive the filling time from h1h_1 to h2h_2.

  2. Evaluate the time for H=1.0mH=1.0\,\mathrm{m}, R=0.50mR=0.50\,\mathrm{m}, Q=1.0×10−3m3/sQ=1.0\times10^{-3}\,\mathrm{m^3/s}, h1=0.20mh_1=0.20\,\mathrm{m} and h2=0.60mh_2=0.60\,\mathrm{m}. Explain the formal behavior as h→0h\to0.

Question 6 - Solution

A conical tank rises quickly near its tip

Diagram shown in the original SVG worksheet.

(a) Derivation and calculation

Similar triangles give r(h)=Rh/Hr(h)=Rh/H, henceA(h)=πR2h2/H2,Q=dVdt=A(h)dhdt.A(h)=\pi R^2h^2/H^2,\quad Q=\frac{dV}{dt}=A(h)\frac{dh}{dt}.dhdt=QH2πR2h2.\boxed{\frac{dh}{dt}=\frac{QH^2}{\pi R^2h^2}}.Δt=πR2QH2∫h1h2h2dh=πR2(h23−h13)3QH2.\Delta t=\frac{\pi R^2}{QH^2}\int_{h_1}^{h_2}h^2\,dh=\boxed{\frac{\pi R^2(h_2^3-h_1^3)}{3QH^2}}.

(b) Result and interpretation

Δt=π(.500)2(.6003−.2003)3(.00100)(1.00)2=54.4543s.\boxed{\Delta t=\frac{\pi(.500)^2(.600^3-.200^3)}{3(.00100)(1.00)^2}=54.4543\,\mathrm s}.h→0+:A(h)→0,dh/dt→∞,Q=finite.h\to0^+:\quad A(h)\to0,\quad dh/dt\to\infty,\quad Q=\text{finite}.The divergence concerns height rate, not incoming volume rate; finite inlet geometry and wetting limit the tip idealization.

Physical check

The same time follows from [V(h2)−V(h1)]/Q[V(h_2)-V(h_1)]/Q with V(h)=πR2h3/(3H2)V(h)=\pi R^2h^3/(3H^2).