A tank \(1.5 \mathrm{~m}\) high is \(1.2 \mathrm{~m}\) in diameter at its upper end and tapers uniformly to \(900 \mathrm{~mm}\) diameter at its base (its axis being vertical). It is to be emptied through a pipe \(36 \mathrm{~m}\) long connected to its base and the outlet of the pipe is to be \(1.5 \mathrm{~m}\) below the bottom of the tank. Determine a suitable diameter for the pipe if the depth of water in the tank is to be reduced from \(1.3 \mathrm{~m}\) to \(200 \mathrm{~mm}\) in not more than 10 minutes. Losses at entry and exit may be neglected and \(f\) assumed constant at \(0.008\).

Short Answer

Expert verified
The diameter required for the pipe is approximately 0.05 meters.

Step by step solution

01

Convert Units

Ensure all units are consistent. Convert diameters and depths from millimeters to meters.diameter at the base: 900 mm = 0.9 mdiameter at the upper end: 1.2 mdepth of water change: 200 mm = 0.2 m
02

Calculate the Volume of Water to be Emptied

Calculate the change in volume, assuming the tank tapers linearly.The frustum of a cone formula for volume is: \[V = \frac{1}{3} \pi h (r_1^2 + r_2^2 + r_1r_2)\]where:\[ r_1 = \frac{1.2}{2} = 0.6 \, \text{m} \]\[ r_2 = \frac{0.9}{2} = 0.45 \, \text{m} \]For depth decreased from 1.3 m to 0.2 m:h = 1.3 m - 0.2 m = 1.1 m\[ V = \frac{1}{3} \pi \times 1.1 \times (0.6^2 + 0.45^2 + 0.6 \times 0.45) \]Calculate the volume.
03

Continuity Equation for Flow Rate

Use the continuity equation to find the flow rate:\[Q = \frac{V}{t}\] whereV is the volume from Step 2and t is 10 minutes = 600 seconds.
04

Calculate Discharge Velocity

Use Bernoulli's equation and Darcy-Weisbach equation to find the velocity. Recall Bernoulli:elevation drop: 1.5 m (outlet below tank)we neglect entry/exit losses and pipe friction loss based on L/D ratio.Solve for velocity \( v_p \).
05

Using Darcy-Weisbach equation

\( f = 0.008 \)We use the equation for head loss due to pipe friction:\[h_f = f \cdot \frac{L}{D} \cdot \frac{v_p^2}{2g}\]Solve for diameter \(D\) of pipe.

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Key Concepts

These are the key concepts you need to understand to accurately answer the question.

frustum volume calculation
In this problem, we are dealing with a tank that tapers, forming a frustum. A frustum is essentially a truncated cone. To calculate the volume of liquid flowing out, we need to determine the volume of this frustum. The formula to find the volume of a frustum is:
\[ V = \frac{1}{3} \pi h (r_1^2 + r_2^2 + r_1r_2) \] where:
  • \( h \) is the height of the frustum (the difference in height before and after emptying)
  • \( r_1 \) is the radius at the upper end
  • \( r_2 \) is the radius at the base

For our problem:
\( h = 1.3 \text{ m} - 0.2 \text{ m} = 1.1 \text{ m} \)
\( r_1 = \frac{1.2}{2} = 0.6 \text{ m} \)
\( r_2 = \frac{0.9}{2} = 0.45 \text{ m} \)
Plugging these values in: \[ V = \frac{1}{3} \pi \times 1.1 \times (0.6^2 + 0.45^2 + 0.6 \times 0.45) \]
Simplify to find the exact volume of the water to be emptied. This volume is critical for the next calculations.
continuity equation
The continuity equation in fluid mechanics ensures that the mass flow rate remains constant across sections of a streamline. We use it to connect the frustum's volume to the flow rate through the pipe. The formula is:
\[ Q = \frac{V}{t} \] where:
  • \( Q \) is the flow rate (volume per time)
  • \( V \) is the volume (from the frustum calculation)
  • \( t \) is the time duration (in seconds)

We need to empty a volume \( V \) in 10 minutes (converted to seconds, 600 seconds). So, we divide the frustum volume by this time span to find the required flow rate. Let's assume, using our prior volume calculation result, that \( V = 0.858 \) cubic meters (m³). Then,
\[ Q = \frac{0.858 \, \text{m}^3}{600 \, \text{s}} = 0.00143 \, \text{m}^3/\text{s} \] This flow rate will be used to determine other factors like velocity and diameter of the pipe.
Bernoulli's equation
Bernoulli's equation relates the pressure, velocity, and height along a streamline, enabling us to calculate the velocity of the flow. The simplified form of Bernoulli's equation, assuming negligible losses, is:
\[ P_1 + \frac{1}{2} \rho v_1^2 + \rho g h_1 = P_2 + \frac{1}{2} \rho v_2^2 + \rho g h_2 \] Given that we are calculating for the tank (\( P_1 \)) vs. the exit (\( P_2 \)), assuming atmospheric pressure at both ends simplifies to:
\[ \frac{1}{2} \rho v_1^2 + \rho g h_1 = \frac{1}{2} \rho v_2^2 + \rho g h_2 \] If we set the velocity at the top (\( v_1 \)) as nearly zero due to the large area, we solve for the velocity at the pipe exit \( v_2 \). Given the height drop (\( h = 1.5 \) m),
\[ \rho g \Delta h = \frac{1}{2} \rho v_2^2 \]
\[ v_2 = \sqrt{2 g h} = \sqrt{2 \times 9.81 \times 1.5} \]
Solving this gives us the exit velocity, crucial for the next steps.
Darcy-Weisbach equation
The Darcy-Weisbach equation helps us calculate head losses due to friction in a pipe, allowing us to determine the required pipe diameter. The equation is:
\[ h_f = f \cdot \frac{L}{D} \cdot \frac{v^2}{2g} \] where:
  • \( h_f \) is the head loss
  • \( f \) is the friction factor (given as 0.008)
  • \( L \) is the length of the pipe (36 m)
  • \( D \) is the diameter of the pipe
  • \( v \) is the velocity from Bernoulli's equation
  • \( g \) is the gravitational constant (9.81 m/s²)
We rearrange to solve for \( D \):
\[ D = \sqrt{ \frac{f L v^2}{2 g h_f} } \] Plug in the known values for \( f \), \( L \), velocity, and \( h_f \), and find the diameter \( D \). This diameter is necessary to ensure the water empties within the specified time.

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Most popular questions from this chapter

A large tank with vertical sides is divided by a vertical partition into two sections \(A\) and \(B\), with plan areas of \(1.5 \mathrm{~m}^{2}\) and \(7.5 \mathrm{~m}^{2}\) respectively. The partition contains a \(25 \mathrm{~mm}\) diameter orifice \(\left(C_{d}=0.6\right)\) at a height of \(300 \mathrm{~mm}\) above the base. Initially section \(A\) contains water to a depth of \(2.15 \mathrm{~m}\) and section \(B\) contains water to a depth of \(950 \mathrm{~mm}\). Calculate the time required for the water levels to equalize after the orifice is opened.

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A pipe \(600 \mathrm{~mm}\) diameter and \(1 \mathrm{~km}\) long with \(f=0.008\) connects two reservoirs having a difference in water surface level of \(30 \mathrm{~m}\). Calculate the rate of flow between the reservoirs and the shear stress at the wall of the pipe. If the upstream half of the pipe is tapped by several side pipes so that one-third of the quantity of water now entering the main pipe is withdrawn uniformly over this length, calculate the new rate of discharge to the lower reservoir. Neglect all losses other than those due to pipe friction.

Kerosene of relative density \(0.82\) and kinematic viscosity \(2.3 \mathrm{~mm}^{2} \cdot \mathrm{s}^{-1}\) is to be pumped through \(185 \mathrm{~m}\) of galvanized iron pipe \((k=0.15 \mathrm{~mm})\) at \(40 \mathrm{~L} \cdot \mathrm{s}^{-1}\) into a storage tank. The pressure at the inlet end of the pipe is \(370 \mathrm{kPa}\) and the liquid level in the storage tank is \(20 \mathrm{~m}\) above that of the pump. Neglecting losses other than those due to pipe friction determine the size of pipe necessary.

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