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What can be deduced from energy and entropy balances about a system undergoing a thermodynamic cycle while receiving energy by heat transfer at temperature \(T_{\mathrm{C}}\) and discharging energy by heat transfer at a higher temperature \(T_{\mathrm{H}}\), if these are the only energy transfers the system experiences?

Short Answer

Expert verified
From energy and entropy balances, for a system discharging heat at \(T_{\mathrm{H}}\) and receiving heat at \(T_{\mathrm{C}}\), the net work done is: \[ W = Q_{\mathrm{H}} \left( \frac{T_{\mathrm{C}} - T_{\mathrm{H}}}{T_{\mathrm{H}}} \right) \].

Step by step solution

01

Identify the Heat Transfer Temperatures

Note that the system receives energy by heat transfer at temperature \(T_{\mathrm{C}}\) and discharges energy by heat transfer at a higher temperature \(T_{\mathrm{H}}\).
02

Apply the First Law of Thermodynamics

By the First Law of Thermodynamics (conservation of energy), the net work done by the system over one complete cycle is the difference between the heat received and the heat discharged. Let the heat received be \(Q_{\mathrm{C}}\) and the heat discharged be \(Q_{\mathrm{H}}\). The work done, \(W\), is given by: \[ W = Q_{\mathrm{C}} - Q_{\mathrm{H}} \]
03

Consider the Second Law of Thermodynamics

Using the Second Law of Thermodynamics, the net entropy change of the system over one complete cycle is zero since entropy is a state function. For the heat received and discharged, the entropy change can be represented as: \[ \Delta S = \frac{Q_{\mathrm{C}}}{T_{\mathrm{C}}} - \frac{Q_{\mathrm{H}}}{T_{\mathrm{H}}} \]Since the system undergoes a cyclic process, \( \Delta S = 0 \). Thus: \[ \frac{Q_{\mathrm{C}}}{T_{\mathrm{C}}} = \frac{Q_{\mathrm{H}}}{T_{\mathrm{H}}} \]
04

Solve for the Relationship Between Heats

From the entropy balance, solve for the relationship between the heat transfers: \[ Q_{\mathrm{C}} = Q_{\mathrm{H}} \frac{T_{\mathrm{C}}}{T_{\mathrm{H}}} \]This shows that the heat received by the system is scaled by the ratio of the temperatures.
05

Combine Results from Both Laws

Using the work done and the relationship between heat transfers, \[ W = Q_{\mathrm{C}} - Q_{\mathrm{H}} \]Substituting the value of \(Q_{\mathrm{C}}\) from the above entropy balance equation: \[ W = Q_{\mathrm{H}} \left( \frac{T_{\mathrm{C}}}{T_{\mathrm{H}}} \right) - Q_{\mathrm{H}} = Q_{\mathrm{H}} \left( \frac{T_{\mathrm{C}} - T_{\mathrm{H}}}{T_{\mathrm{H}}} \right) \]This relationship indicates the maximum work obtainable from the system.

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Key Concepts

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

First Law of Thermodynamics
The First Law of Thermodynamics is often referred to as the law of energy conservation. It's one of the most fundamental principles of physics. It states that energy cannot be created or destroyed, only transformed from one form to another. In the context of our thermodynamic cycle, this law implies that the net work done by the system is the difference between the energy (in the form of heat) that the system receives and the energy that it discharges. Let's break this down. If we denote the heat received by the system as \(Q_C\) and the heat discharged as \(Q_H\), then the work done \(W\) by the system over one complete cycle can be expressed as:
\[ W = Q_C - Q_H \] This equation tells us that the work output is fundamentally tied to the difference between heat input and heat output. No matter what processes the system undergoes, energy conservation must always hold true.
Second Law of Thermodynamics
The Second Law of Thermodynamics introduces the concept of entropy, a measure of the system's energy dispersal or disorder. Entropy always increases or remains stable for processes in an isolated system. In a thermodynamic cycle, the system reaches a state where the net entropy change over one complete cycle is zero. This is because entropy is a state function - it depends only on the state of the system, not on how it got there.
For our system, where heat is received at temperature \(T_C\) and discharged at a higher temperature \(T_H\), the entropy change can be shown as: \[ \frac{Q_C}{T_C} - \frac{Q_H}{T_H} \] Since the system undergoes a complete cycle, the net entropy change \(\Delta S = 0\). This gives us:
\[ \frac{Q_C}{T_C} = \frac{Q_H}{T_H} \] This relation is crucial because it ties together the amounts of heat transfer with the temperatures at which these transfers occur.
Entropy Balance
Entropy balance is a valuable tool for analyzing thermodynamic processes. As mentioned earlier, for a complete cycle in a thermodynamic system, the net entropy change must be zero. This is practically useful because it sets a relationship between the heat exchanges and the temperatures involved. Let's further explore this:
  • From the Second Law, we already have \[ \frac{Q_C}{T_C} = \frac{Q_H}{T_H} \]
  • Simplifying this, we can rearrange to find \[ Q_C = Q_H \frac{T_C}{T_H} \]
This implies that the heat received by the system (\(Q_C\)) is directly proportional to the temperature ratio \(T_C/T_H\). We can use this relationship in conjunction with the First Law to find the work output. Substituting \(Q_C\) in our work equation:
  • \[ W = Q_C - Q_H \]
  • \[ W = Q_H \frac{T_C}{T_H} - Q_H \]
  • \[ W = Q_H \frac{T_C - T_H}{T_H} \]
This result shows the maximum work obtainable from the system, tying together all the principles of energy and entropy balance.

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Most popular questions from this chapter

At steady state, a device receives a stream of saturated water vapor at \(210^{\circ} \mathrm{C}\) and discharges a condensate stream at \(20^{\circ} \mathrm{C}, 0.1 \mathrm{MPa}\) while delivering energy by heat transfer at \(300^{\circ} \mathrm{C}\). The only other energy transfer involves heat transfer at \(20^{\circ} \mathrm{C}\) to the surroundings. Kinetic and potential energy changes are negligible. What is the maximum theoretical amount of energy, in \(\mathrm{kJ}\) per \(\mathrm{kg}\) of steam entering, that could be delivered at \(300^{\circ} \mathrm{C} ?\)

A 5-kilowatt pump operating at steady state draws in liquid water at 1 bar, \(15^{\circ} \mathrm{C}\) and delivers it at 5 bar at an elevation \(6 \mathrm{~m}\) above the inlet. There is no significant change in velocity between the inlet and exit, and the local acceleration of gravity is \(9.8 \mathrm{~m} / \mathrm{s}^{2} .\) Would it be possible to pump \(7.5 \mathrm{~m}^{3}\) in \(10 \mathrm{~min}\) or less? Explain.

A system consists of \(2 \mathrm{~m}^{3}\) of hydrogen gas \(\left(\mathrm{H}_{2}\right)\), initially at \(35^{\circ} \mathrm{C}, 215 \mathrm{kPa}\), contained in a closed rigid tank. Energy is transferred to the system from a reservoir at \(300^{\circ} \mathrm{C}\) until the temperature of the hydrogen is \(160^{\circ} \mathrm{C}\). The temperature at the system boundary where heat transfer occurs is \(300^{\circ} \mathrm{C}\). Modeling the hydrogen as an ideal gas, determine the heat transfer, in \(\mathrm{kJ}\), the change in entropy, in \(\mathrm{kJ} / \mathrm{K}\), and the amount of entropy produced, in \(\mathrm{kJ} / \mathrm{K}\). For the reservoir, determine the change in entropy, in \(\mathrm{kJ} / \mathrm{K}\). Why do these two entropy changes differ?

Steam is contained in a large vessel at \(100 \mathrm{lbf} / \mathrm{in} .^{2}, 450^{\circ} \mathrm{F}\). Connected to the vessel by a valve is an initially evacuated tank having a volume of \(1 \mathrm{ft}^{3}\). The valve is opened until the tank is filled with steam at pressure \(p\). The filling is adiabatic, kinetic and potential energy effects are negligible, and the state of the large vessel remains constant. (a) If \(p=100 \mathrm{lbf} / \mathrm{in} .^{2}\), determine the final temperature of the steam within the tank, in \({ }^{\circ} \mathrm{F}\), and the amount of entropy produced within the tank, in \(\mathrm{Btu} /{ }^{\circ} \mathrm{R}\). (b) Plot the quantities of part (a) versus presssure \(p\) ranging from 10 to \(100 \mathrm{lbf} / \mathrm{in}\).

Air enters an insulated compressor operating at steady state at \(0.95\) bar, \(27^{\circ} \mathrm{C}\) with a mass flow rate of \(4000 \mathrm{~kg} / \mathrm{h}\) and exits at \(8.7\) bar. Kinetic and potential energy effects are negligible. (a) Determine the minimum theoretical power input required, in \(\mathrm{kW}\), and the corresponding exit temperature, in \({ }^{\circ} \mathrm{C}\). (b) If the exit temperature is \(347^{\circ} \mathrm{C}\), determine the power input, in \(\mathrm{kW}\), and the isentropic compressor efficiency.

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