Warning: foreach() argument must be of type array|object, bool given in /var/www/html/web/app/themes/studypress-core-theme/template-parts/header/mobile-offcanvas.php on line 20

Water is to be pumped from a lake to a reservoir located on a bluff \(290 \mathrm{ft}\) above. According to the specifications, the piping is Schedule 40 steel pipe having a nominal diameter of 1 inch and the volumetric flow rate is \(10 \mathrm{gal} / \mathrm{min}\). The total length of pipe is \(580 \mathrm{ft}\). A centrifugal pump is specified. Estimate the electrical power required by the pump, in \(\mathrm{kW}\). Is a centrifugal pump a good choice for this application? What precautions should be taken to avoid cavitation?

Short Answer

Expert verified
The estimated electrical power required is 26.4 kW. A centrifugal pump is a good choice for this application. To avoid cavitation, maintain proper suction conditions and monitor pump speed.

Step by step solution

01

Convert volumetric flow rate to cubic feet per second (cfs)

Convert the given volumetric flow rate from gallons per minute (gal/min) to cubic feet per second (cfs). Use the conversion factors: \(1 \text{ gal} = 0.1337 \text{ ft}^3\) and \(1 \text{ min} = 60 \text{ s}\). The flow rate is \(10 \text{ gal/min}\). Calculation: \[ Q = 10 \text{ gal/min} \times 0.1337 \text{ ft}^3/\text{gal} \times \frac{1}{60} \text{ min/s} = 0.0223 \text{ ft}^3/s \]
02

Calculate the head loss due to elevation (static head)

The static head is the vertical distance the water needs to be pumped. In this case, it's 290 feet (the elevation difference).\[ h_{static} = 290 \text{ ft} \]
03

Calculate the Reynolds number to determine the flow regime

Reynolds number is calculated to determine if the flow is laminar or turbulent.First, estimate the velocity ( v ) in the pipe:\[ v = \frac{Q}{A} = \frac{0.0223 \text{ ft}^3/s}{ \frac{\text{π} (0.5 \text{ in})^2}{144} \text{ ft}^2} = 3.65 \text{ ft/s} \]Where inner diameter is 1 inch and area is \( A = \frac{\text{π} D^2}{4}\).Then use the kinematic viscosity ( u ) of water (1.22 \times 10^{-5} \text{ ft}^2/\text{s}): \[ \text{Re} = \frac{v \times D}{u} = \frac{3.65 \text{ ft/s} \times 0.0833 \text{ ft}}{1.22 \times 10^{-5} \text{ ft}^2/\text{s}} = 2.49 \times 10^4 \]
04

Determine the friction factor

Since the flow is turbulent (Re > 4000), use the Darcy-Weisbach equation and Moody chart or Colebrook equation for turbulent flow in smooth pipes:Assume roughness factor ( \text{k} ): \[ f = 0.02 \]
05

Calculate the head loss due to friction

Using Darcy-Weisbach equation:\[ h_f = f \frac{L}{D} \frac{v^2}{2g} = 0.02 \frac{580 \text{ ft}}{0.0833 \text{ ft}} \frac{(3.65 \text{ ft/s})^2}{2 \times 32.2 \text{ ft/s}^2 } = 35 \text{ ft} \]
06

Calculate the total head required

Total head required ( h_{total} ) is the sum of static head and head loss due to friction:\[ h_{total} = h_{static} + h_f = 290 \text{ ft} + 35 \text{ ft} = 325 \text{ ft} \]
07

Calculate the hydraulic power

Hydraulic power ( P_{hyd} ) required to lift water to 325 feet: \[ P_{hyd} = \rho g Q h_{total} \rho = 62.4 \text{ lb/ft}^3 \] \[ P_{hyd} = 62.4 \text{ lb/ft}^3 \times 32.2 \text{ ft/s}^2 \times 0.0223 \text{ ft}^3/s \times 325 \text{ ft} = 14,579.7 \text{ ft-lb/s} \]Convert to kilowatt ( \text{kW} ):\[ 1 \text{ kW} = 737.56 \text{ ft-lb/s } \] \[ P_{hyd} = \frac{14,579.7 \text{ ft-lb/s}}{737.56} = 19.8 \text{ kW} \]
08

Estimate the electrical power requirement

Determine the electrical power considering the pump efficiency ( \text{η} ), assume pump efficiency as 75% (0.75):\[ P_{elec} = \frac{P_{hyd}}{\text{η}} = \frac{19.78 \text{ kW}}{0.75} = 26.4 \text{ kW} \]
09

Evaluate if centrifugal pump is a good choice

Centrifugal pumps are generally good for large discharge and lower head requirements. For a head of 325 feet, centrifugal pumps should be adequate, especially if they are high head types.
10

Precautions to avoid cavitation

To avoid cavitation:1. Ensure the suction pipe is short and has minimal elevation difference.2. Keep the suction pressure above the vapor pressure of the fluid.3. Maintain proper pump speed.4. Install an air release valve if necessary.

Unlock Step-by-Step Solutions & Ace Your Exams!

  • Full Textbook Solutions

    Get detailed explanations and key concepts

  • Unlimited Al creation

    Al flashcards, explanations, exams and more...

  • Ads-free access

    To over 500 millions flashcards

  • Money-back guarantee

    We refund you if you fail your exam.

Over 30 million students worldwide already upgrade their learning with Vaia!

Key Concepts

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

Water Flow Rate
The water flow rate indicates how much water is being transferred over a certain period. It is often measured in gallons per minute (gal/min) or cubic feet per second (cfs). The exercise gives a flow rate of 10 gal/min. Converting this to cfs helps simplify further calculations. The conversion is performed by recognizing that 1 gallon equals 0.1337 cubic feet and 1 minute contains 60 seconds, resulting in an ultimate rate of: \( Q = 10 \text{ gal/min} \times 0.1337 \text{ ft}^3/\text{gal} \times \frac{1}{60} \text{ min/s} = 0.0223 \text{ ft}^3/s \)
Static Head
The static head represents the vertical height the water needs to be pumped from one elevation to another. It is a primary component in calculating the total head. In this exercise, the water needs to be pumped 290 feet above the starting point. This elevation difference directly affects the energy required to move the water. Expressed mathematically: \( h_{\text{static}} = 290 \text{ ft} \)
Reynolds Number
The Reynolds Number (Re) helps determine the type of flow within the pipe—whether it’s laminar or turbulent. Re is calculated using the velocity of the water, the pipe's diameter, and the water’s kinematic viscosity. First, we calculate the velocity ( v ) using: \( v = \frac{Q}{A} = \frac{0.0223 \text{ ft}^3/s}{\frac{\text{π} (0.5 \text{ in})^2}{144} \text{ ft}^2} = 3.65 \text{ ft/s} \) Here A is the cross-sectional area of the pipe. Then, the Reynolds Number is calculated as: \( \text{Re} = \frac{v \times D}{u} = \frac{3.65 \text{ ft/s} \times 0.0833 \text{ ft}}{1.22 \times 10^{-5} \text{ ft}^2/\text{s}} = 2.49 \times 10^4 \)
Friction Factor
The friction factor ( f ) is crucial for determining the head loss due to pipe friction. Since our flow is turbulent (Re > 4000), we use the Darcy-Weisbach equation, often simplifying with the Moody chart or Colebrook equation. For this exercise, we assume a roughness factor ( k ) and select: \( f = 0.02 \)
Darcy-Weisbach Equation
The Darcy-Weisbach equation estimates the head loss ( h_f ) due to friction within the pipe. The formula used is: \( h_f = f \frac{L}{D} \frac{v^2}{2g} = 0.02 \frac{580 \text{ ft}}{0.0833 \text{ ft}} \frac{(3.65 \text{ ft/s})^2}{2 \times 32.2 \text{ ft/s}^2 } = 35 \text{ ft} \) Here, L is the pipe length, D is the diameter, v is the velocity, g is gravitational acceleration, and f is the friction factor.
Hydraulic Power
Hydraulic power ( P_{\text{hyd}} ) measures the energy needed by the water to overcome elevation and friction losses. It is computed using the water density ( ρ ), gravitational acceleration ( g ), water flow rate ( Q ), and the total head ( h_{\text{total}} ). \( P_{\text{hyd}} = ρ g Q h_{\text{total}} \) Plugging in the numbers: \( P_{\text{hyd}} = 62.4 \text{ lb/ft}^3 \times 32.2 \text{ ft/s}^2 \times 0.0223 \text{ ft}^3/s \times 325 \text{ ft} = 14579.7 \text{ ft-lb/s} \)
Pump Efficiency
Pump efficiency ( η ) is a measure of how effectively the pump converts electrical power into hydraulic power. A pump’s efficiency plays a vital role in determining the electrical power requirement. Using an assumed pump efficiency of 75% (0.75), the electrical power needed ( P_{\text{elec}} ) is given by: \( P_{\text{elec}} = \frac{P_{\text{hyd}}}{η} = \frac{19.78 \text{ kW}}{0.75} = 26.4 \text{ kW} \)
Cavitation Prevention
Cavitation is a common problem that occurs when the water pressure drops below its vapor pressure, leading to the formation of bubbles that can damage the pump. Preventing cavitation is crucial for maintaining pump longevity. Here are a few precautions:
  • Ensure the suction pipe is as short and direct as possible.
  • Keep the suction pressure above the water's vapor pressure.
  • Maintain appropriate pump speeds.
  • Install air release valves if necessary.
By following these precautions, you can help to avoid the damaging effects of cavitation.

One App. One Place for Learning.

All the tools & learning materials you need for study success - in one app.

Get started for free

Most popular questions from this chapter

Air enters an insulated compressor operating at steady state at 1 bar, \(350 \mathrm{~K}\) with a mass flow rate of \(1 \mathrm{~kg} / \mathrm{s}\) and exits at 4 bar. The isentropic compressor efficiency is \(82 \%\). Determine the power input, in \(\mathrm{kW}\), and the rate of entropy production, in \(\mathrm{kW} / \mathrm{K}\), using the ideal gas model with (a) data from Table A-22. (b) \(I T\). (c) a constant specific heat ratio, \(k=1.39\).

How can entropy be transferred into, or out of, a closed system? A control volume?

Air enters a compressor operating at steady state with a volumetric flow rate of \(8 \mathrm{~m}^{3} / \mathrm{min}\) at \(23^{\circ} \mathrm{C}, 0.12 \mathrm{MPa}\). The air is compressed isothermally without internal irreversibilities, exiting at \(1.5 \mathrm{MPa}\). Kinetic and potential energy effects can be ignored. Evaluate the work required and the heat transfer, each in \(\mathrm{kW}\).

Carbon monoxide enters a nozzle operating at steady state at \(5 \mathrm{bar}, 200^{\circ} \mathrm{C}, 1 \mathrm{~m} / \mathrm{s}\) and undergoes a polytropic expansion to 1 bar with \(n=1.2\). Using the ideal gas model and ignoring potential energy effects, determine (a) the exit velocity, in \(\mathrm{m} / \mathrm{s}\). (b) the rate of heat transfer between the gas and its surroundings, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of gas flowing.

A reversible refrigeration cycle \(\mathrm{R}\) and an irreversible refrigeration cycle I operate between the same two reservoirs and each removes \(Q_{\mathrm{C}}\) from the cold reservoir. The net work input required by \(\mathrm{R}\) is \(W_{\mathrm{R}}\), while the net work input for \(\mathrm{I}\) is \(W_{\mathrm{I}}\). The reversible cycle discharges \(Q_{\mathrm{H}}\) to the hot reservoir, while the irreversible cycle discharges \(Q_{\mathrm{H}}^{\prime}\). Show that \(W_{1}>W_{\mathrm{R}}\) and \(Q_{\mathrm{H}}^{\prime}>Q_{\mathrm{H}}\).

See all solutions

Recommended explanations on Physics Textbooks

View all explanations

What do you think about this solution?

We value your feedback to improve our textbook solutions.

Study anywhere. Anytime. Across all devices.

Sign-up for free