/*! This file is auto-generated */ .wp-block-button__link{color:#fff;background-color:#32373c;border-radius:9999px;box-shadow:none;text-decoration:none;padding:calc(.667em + 2px) calc(1.333em + 2px);font-size:1.125em}.wp-block-file__button{background:#32373c;color:#fff;text-decoration:none} Problem 182 An electrically driven pump oper... [FREE SOLUTION] | 91Ó°ÊÓ

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An electrically driven pump operating at steady state draws water from a pond at a pressure of 1 bar and a rate of \(50 \mathrm{~kg} / \mathrm{s}\) and delivers the water at a pressure of 4 bar. There is no significant heat transfer with the surroundings, and changes in kinetic and potential energy can be neglected. The isentropic pump efficiency is \(75 \%\). Evaluating electricity at \(8.5\) cents per \(\mathrm{kW} \cdot \mathrm{h}\), estimate the hourly cost of running the pump.

Short Answer

Expert verified
The hourly cost of running the pump is $1.70.

Step by step solution

01

- Understand the problem

A pump operates by moving water from a low pressure to a higher pressure. We need to find the hourly cost of running the pump, given the efficiency and electricity cost per kWh. Neglect heat transfer and changes in kinetic/potential energy.
02

- Determine work done by the pump

Use the formula for work done by a pump per unit mass of fluid: \[ W_{\text{pump,ideal}} = \frac{(P_2 - P_1)}{\rho} \] where \( P_1 = 1 \text{ bar} = 10^5 \text{ Pa} \) \( P_2 = 4 \text{ bar} = 4 \times 10^5 \text{ Pa} \) \( \rho \text{ (density of water)} \) = \( 1000 \text{ kg/m}^3 \)}
03

- Calculate Work Done by Ideal Pump

Substitute the values into the formula: \[ W_{\text{pump,ideal}} = \frac{(4 \times 10^5 \text{ Pa} - 10^5 \text{ Pa})}{1000 \text{ kg/m}^3} = \frac{3 \times 10^5}{1000} \text{ J/kg} = 300 \text{ J/kg} \]
04

- Adjust for pump efficiency

The actual work required will be more due to efficiency: \[ W_{\text{pump}} = \frac{W_{\text{pump,ideal}}}{\text{efficiency}} = \frac{300 \text{ J/kg}}{0.75} = 400 \text{ J/kg} \]
05

- Calculate total power required

Given the mass flow rate of \( \frac{dm}{dt} = 50 \text{ kg/s}\), total power\( \text{(in W)} \) required is: \[ P = W_{\text{pump}} \times \frac{dm}{dt} = 400 \text{ J/kg} \times 50 \text{ kg/s} = 20000 \text{ W} \] We can convert this to kW: \[ P = 20000 \text{ W} = 20 \text{ kW} \]
06

- Calculate hourly cost of running the pump

Using the cost of electricity: \[ \text{hourly cost} = P \times \text{cost per kW}\times h = 20 \text{ kW} \times 8.5 \text{ cents/kW} \times \text{1 hour} \] Convert to dollars: \[ \text{cost} = 20 \times 8.5 \times 0.01 = 1.70 \text{ dollars/hour} \]

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Key Concepts

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

isentropic efficiency
The term 'isentropic efficiency' describes how well a pump, compressor, or turbine operates compared to an ideal version of that device.
An ideal pump or compressor increases the pressure of a fluid in a perfectly efficient manner. Real-world devices, however, are not perfectly efficient.
The formula for isentropic efficiency (\( \eta_S \)) is:
\[ \eta_S = \frac{W_{\text{ideal}}}{W_{\text{actual}}} \]
Here, \( W_{\text{ideal}} \) represents the work an ideal pump would do, and \( W_{\text{actual}} \) represents the actual work done, considering losses due to friction and heat.
In this exercise, the given isentropic efficiency is 75%, meaning the pump operates at 75% of the efficiency of an ideal pump.
work done by pump
To understand the work done by the pump, let's first look at the formula provided:
\[ W_{\text{pump,ideal}} = \frac{(P_2 - P_1)}{\rho} \]
This formula calculates the work done by an ideal pump per unit mass of fluid.
In our problem, \( P_1 \) is 1 bar and \( P_2 \) is 4 bar.
After converting these pressures to Pascals and using the density of water (\( \rho = 1000 \, \text{kg/m}^3 \)), we find:
\[ W_{\text{pump,ideal}} = \frac{(4 \times 10^5 \text{ Pa} - 10^5 \text{ Pa})}{1000 \text{ kg/m}^3} = 300 \text{ J/kg} \]
However, the actual work done by the pump is higher because of the pump's efficiency.
The formula to find the actual work done is:
\[ W_{\text{pump}} = \frac{W_{\text{pump,ideal}}}{\eta_S} \]
Substituting the values gives us:
\[ W_{\text{pump}} = \frac{300 \text{ J/kg}}{0.75} = 400 \text{ J/kg} \]
This adjustment takes into account the pump’s isentropic efficiency.
cost of electricity
The cost of operating an electrically driven pump is influenced by the electricity rate and the pump's power consumption.
The power required can be calculated using the actual work done by the pump and the flow rate:
\[ P = W_{\text{pump}} \times \frac{dm}{dt} \]
With an actual work of 400 J/kg and flow rate of 50 kg/s:
\[ P = 400 \text{ J/kg} \times 50 \text{ kg/s} = 20000 \text{ W} = 20 \text{ kW} \]
The hourly cost of running the pump is then calculated by multiplying the power consumption by the electricity rate and the operating time.
Here, the electricity cost is given as 8.5 cents per kWh.
Therefore, the hourly cost is:
\[ \text{cost} = P \times \text{rate per kW} \times h \]
\[ \text{cost} = 20 \text{ kW} \times 8.5 \text{ cents/kW} \times 1 \text{ hour} \]
Converting to dollars:
\[ \text{cost} = 20 \times 8.5 \times 0.01 = 1.70 \text{ dollars/hour} \]
This means it costs $1.70 per hour to run the pump under the given conditions.

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Most popular questions from this chapter

Air enters a turbine operating at steady state at \(500 \mathrm{kPa}\), \(860 \mathrm{~K}\) and exits at \(100 \mathrm{kPa}\). A temperature sensor indicates that the exit air temperature is \(460 \mathrm{~K}\). Stray heat transfer and kinetic and potential energy effects are negligible, and the air can be modeled as an ideal gas. Determine if the exit temperature reading can be correct. It yes, determine the power developed by the turbine for an expansion between these states, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of air flowing. If no, provide an explanation with supporting calculations.

Oxygen \(\left(\mathrm{O}_{2}\right)\) at \(25^{\circ} \mathrm{C}, 100 \mathrm{kPa}\) enters a compressor operating at steady state and exits at \(260^{\circ} \mathrm{C}, 650 \mathrm{kPa}\). Stray heat transfer and kinetic and potential energy effects are negligible. Modeling the oxygen as an ideal gas with \(k=\) \(1.379\), determine the isentropic compressor efficiency and the work in kJ per kg of oxygen flowing.

Water vapor at \(6 \mathrm{MPa}, 600^{\circ} \mathrm{C}\) enters a turbine operating at steady state and expands to \(10 \mathrm{kPa}\). The mass flow rate is \(2 \mathrm{~kg} / \mathrm{s}\), and the power developed is \(2626 \mathrm{~kW}\). Stray heat transfer and kinetic and potential energy effects are negligible. Determine (a) the isentropic turbine efficiency and (b) the rate of entropy production within the turbine, in \(\mathrm{kW} / \mathrm{K}\).

A rigid, insulated tank with a volume of \(21.61 \mathrm{ft}^{3}\) is filled initially with air at \(110 \mathrm{lbf} / \mathrm{in}^{2}, 535^{\circ} \mathrm{R}\). A leak develops, and air slowly escapes until the pressure of the air remaining in the tank is \(15 \mathrm{lbf} / \mathrm{in}^{2}\). Employing the ideal gas model with \(k=1.4\) for the air, determine the amount of mass remaining in the tank, in lb, and its temperature, in \({ }^{\circ} \mathrm{R}\).

Construct a plot, to scale, showing constant-pressure lines of \(5.0\) and \(10 \mathrm{MPa}\) ranging from 100 to \(400^{\circ} \mathrm{C}\) on a \(T-s\) diagram for water.

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