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Reducing irreversibilities within a system can improve its thermodynamic performance, but steps taken in this direction are usually constrained by other considerations. What are some of these?

Short Answer

Expert verified
Constraints include financial, technological, physical/material, operational/maintenance, and safety/environmental factors.

Step by step solution

01

- Define Irreversibilities

Irreversibilities in a thermodynamic system refer to the inefficiencies that occur due to factors like friction, unrestrained expansion, mixing of different substances, heat transfer across a finite temperature difference, etc. These reduce the system's performance by increasing entropy and energy losses.
02

- Acknowledge Methods to Reduce Irreversibilities

Several methods can be used to reduce irreversibilities, such as optimizing the design of components, improving insulation, reducing friction through lubrication, and increasing heat exchanger effectiveness.
03

- Identify Practical Constraints

While reducing irreversibilities is beneficial, practical constraints often limit the extent of these improvements. These include:
04

Step 3.1 - Financial Constraints

Implementing advanced materials, better designs, and more efficient processes typically requires significant investment. Budget limitations can restrict the extent of these measures.
05

Step 3.2 - Technological Constraints

Current technological limitations might prevent the complete elimination of irreversibilities. For example, perfect insulation or zero-friction surfaces are not yet achievable with present technology.
06

Step 3.3 - Physical and Material Constraints

Physical properties of materials, such as thermal conductivity and strength, can limit the effectiveness of certain techniques to reduce irreversibility. Additionally, space constraints might limit design modifications.
07

Step 3.4 - Operational and Maintenance Constraints

Modifications that reduce irreversibilities might require more complex operations and maintenance. Increased complexity can result in higher operational and maintenance costs, as well as the need for specialized personnel.
08

Step 3.5 - Safety and Environmental Constraints

Changes to reduce irreversibilities must also consider safety and environmental regulations. Some techniques might have trade-offs that could compromise safety or have adverse environmental impacts.

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Key Concepts

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

Entropy Increase
Entropy is a measure of disorder or randomness in a system. In thermodynamics, an increase in entropy indicates a loss of useful energy. Every real process increases the entropy of the universe, making some energy unavailable for work. Processes like heat transfer, friction, and mixing of different substances all contribute to this increase.
To minimize entropy increase, you can:
  • Optimize heat transfer processes to minimize temperature differences.
  • Use advanced materials with better insulating properties.
  • Improve system designs to reduce friction and turbulence.
While reducing entropy increase can lead to more efficient systems, it is constrained by factors like budget, current technology, and physical material properties.
Energy Losses
Energy losses in a thermodynamic system occur due to irreversibilities, resulting in less efficient performance. Common sources of energy losses include friction, uncontrolled expansions, and heat transfer across temperature gradients.
To reduce energy losses, you can:
  • Implement better insulation to reduce heat losses.
  • Optimize fluid flow to minimize frictional losses.
  • Use more efficient components and design improvements.
These improvements, however, are often constrained by factors such as cost, material limits, and maintenance requirements.
Friction Reduction
Friction is a major source of irreversibility in thermodynamic processes, causing both entropy increase and energy losses. Reducing friction can significantly improve system performance.
Techniques to reduce friction include:
  • Using lubrication to reduce surface friction.
  • Implementing smoother surface finishes on machinery components.
  • Adopting aerodynamic and hydrodynamic designs to streamline fluid flow.
While these methods can reduce friction, practical constraints like financial, physical, and technological limitations often impact their implementation. Effective friction management requires balancing these factors to achieve optimal system performance.
Heat Exchanger Effectiveness
Heat exchangers are crucial for transferring heat between fluids without mixing them. Their effectiveness directly influences the overall efficiency of thermodynamic systems. A more effective heat exchanger minimizes temperature differences between fluids, reducing irreversibilities and energy losses.
To improve heat exchanger effectiveness, consider the following:
  • Optimize design to maximize surface area for heat transfer.
  • Use materials with high thermal conductivity.
  • Maintain clean surfaces to prevent fouling, which reduces efficiency.
Practical limitations such as space, cost, and material properties must be taken into account. Achieving a balance between these constraints and heat exchanger effectiveness is essential for improving system performance.

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Most popular questions from this chapter

Of increasing interest today are turbines, pumps, and heat exchangers that weigh less than 1 gram and have volumes of 1 cubic centimeter or less. Although many of the same design considerations apply to such micromachines as to corresponding full-scale devices, others do not. Of particular interest to designers is the impact of irreversibilities on the performance of such tiny devices. Write a report discussing the influence of irreversibilities related to heat transfer and friction on the design and operation of micromachines.

A piston-cylinder assembly initially contains \(0.1 \mathrm{~m}^{3}\) of carbon dioxide gas at \(0.3\) bar and \(400 \mathrm{~K}\). The gas is compressed isentropically to a state where the temperature is \(560 \mathrm{~K}\). Employing the ideal gas model and neglecting kinetic and potential energy effects, determine the final pressure, in bar, and the work in \(\mathrm{kJ}\), using (a) data from Table A-23. (b) \(I T\) (c) a constant specific heat ratio from Table A-20 at the mean temperature, \(480 \mathrm{~K}\). (d) a constant specific heat ratio from Table A-20 at \(300 \mathrm{~K}\).

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?

The theoretical steam rate is the quantity of steam required to produce a unit amount of work in an ideal turbine. The Theoretical Steam Rate Tables published by The American Society of Mechanical Engineers give the theoretical steam rate in lb per \(\mathrm{kW} \cdot \mathrm{h}\). To determine the actual steam rate, the theoretical steam rate is divided by the isentropic turbine efficiency. Why is the steam rate a significant quantity? Discuss how the steam rate is used in practice.

A gas flows through a one-inlet, one-exit control volume operating at steady state. Heat transfer at the rate \(\dot{Q}_{\mathrm{cv}}\) takes place only at a location on the boundary where the temperature is \(T_{\mathrm{b}}\). For each of the following cases, determine whether the specific entropy of the gas at the exit is greater than, equal to, or less than the specific entropy of the gas at the inlet: (a) no internal irreversibilities, \(\dot{Q}_{\mathrm{cv}}=0\). (b) no internal irreversibilities, \(\dot{Q}_{\mathrm{cv}}<0\). (c) no internal irreversibilities, \(\dot{Q}_{\mathrm{cv}}>0\). (d) internal irreversibilities, \(\dot{Q}_{\mathrm{cv}}<0\). (e) internal irreversibilities, \(\dot{Q}_{\mathrm{cv}} \geq 0\)

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