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Determine the exergy destruction associated with the heat addition process and the expansion process in Prob. \(10-37 .\) Assume a source temperature of \(1600 \mathrm{K}\) and a sink temperature of 285 K. Also, determine the exergy of the steam at the boiler exit. Take \(P_{0}=100 \mathrm{kPa} .\)

Short Answer

Expert verified
- The heat transfer during the heat addition process is \(60.98 kJ/kg\). 2) What is the exergy destruction associated with the heat addition process? - The exergy destruction associated with the heat addition process is \(42.75 kJ/kg\). 3) What is the work output during the expansion process? - The work output during the expansion process is \(7.98 kJ/kg\). 4) What is the exergy destruction associated with the expansion process? - The exergy destruction associated with the expansion process is \(-53 kJ/kg\). 5) What is the exergy of the steam at the boiler exit? - The exergy of the steam at the boiler exit is \(957.17 kJ/kg\).

Step by step solution

01

Heat Transfer During Heat Addition Process

First, we have to find the heat transfer during the heat addition process. It is given as (from Problem 10-37): $$Q_{in}=60.98 kJ/kg$$
02

Exergy Destruction during Heat Addition Process

Now, we can find the exergy destruction during the heat addition process using the following formula: $$Ed_{in} = Q_{in} \left(1-\frac{T_0}{T_{source}}\right)$$ where \(Ed_{in}\) is the exergy destruction during heat addition process, \(T_0\) is the ambient temperature, and \(T_{source}\) is the source temperature. Substitute the given values: $$Ed_{in} = 60.98 \times (1- \frac{285}{1600})$$ $$Ed_{in} \approx 42.75 kJ/kg$$
03

Work during Expansion Process

From Problem 10-37, it is given that: $$W_{out} = 7.98 kJ/kg$$
04

Exergy Destruction during Expansion Process

Now, we can find the exergy destruction during the expansion process using the following formula: $$Ed_{out} = W_{out} - W_{ideal} = W_{out} - Q_{in}$$ where \(Ed_{out}\) is the exergy destruction during expansion process and \(W_{ideal}\) is the ideal work output. Substitute the given values: $$Ed_{out} = 7.98 - 60.98$$ $$Ed_{out} = -53 kJ/kg$$
05

Exergy at the Boiler Exit

Now, we will find the exergy at the boiler exit, which is given by the following formula: $$E_{exit} = u - u_0 - T_0(s - s_0) + P_0(v - v_0)$$ Here, \(E_{exit}\) is the exergy at the boiler exit, \(u, u_0, s, s_0, v, \text{ and } v_0\) are values from table A-2 (superheated steam): \(u = 2776.1 kJ/kg, u_0 = 429.94 kJ/kg, s = 6.5408 kJ/(kg\cdot K), s_0 = 1.6315 kJ/(kg\cdot K), v = 0.5166 m^3/kg, v_0 = 0.001043 m^3/kg\). Now substitute the given values: $$E_{exit} = 2776.1 - 429.94 - (285)(6.5408 - 1.6315) + (100)(0.5166 - 0.001043)$$ $$E_{exit} \approx 957.17 kJ/kg$$ The exergy destruction associated with the heat addition process is \(42.75 kJ/kg\), with the expansion process is \(-53 kJ/kg\), and the exergy of the steam at the boiler exit is \(957.17 kJ/kg\).

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Key Concepts

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

Heat Transfer in Thermodynamics
Understanding heat transfer is fundamental to grasping the concepts of energy efficiency and conservation in thermodynamics. Heat transfer is the movement of thermal energy from one object or substance to another as a result of a temperature difference. This transfer occurs in three main ways: conduction, convection, and radiation.

In thermodynamic systems, such as a steam boiler, heat transfer plays a crucial role during the heat addition process. For instance, in the problem given, heat is added to the system at a rate of 60.98 kJ/kg, increasing the energy within the steam. However, not all of this energy can be converted into useful work. The efficiency of this conversion is affected by the temperature differential between the heat source and the environment, which in the example provided, has a dramatic effect on the exergy destruction during the process.

Understanding how heat transfer affects energy and exergy can help students identify opportunities to improve the efficiency of energy conversion systems. This could involve anything from optimizing temperatures within the system to using insulation to prevent heat loss. The key takeaway is that minimizing exergy destruction is essential for maximizing the efficiency of thermodynamic processes.
Expansion Process in Engines and Turbines
The expansion process is a fundamental concept in thermodynamics, commonly observed in engines and turbines where a working fluid, often steam or gas, expands and does work on the surrounding system. Essentially, as the steam expands, it pushes against the turbine blades or the pistons, converting thermal energy from the heat into mechanical work.

In the given problem, the steam undergoes an expansion process where its volume increases, and it does a work output of 7.98 kJ/kg. An ideal expansion process, often depicted by an isentropic process in idealized thermodynamic cycles, would convert the entire energy available from the heat added into work. However, real-world processes are not perfectly efficient; they are subject to irreversibilities that lead to exergy destruction, which is a measure of lost opportunity to do work.

By analyzing the expansion process in detail, students can gain insights into the real-world efficiency of thermodynamic systems and the importance of reducing irreversibilities to get closer to the ideal behavior. This understanding is crucial when it comes to the design and optimization of engines and turbines for maximum performance and energy conservation.
The Fundamentals of Thermodynamics
Thermodynamics is the science of energy, particularly heat and work, and how they transform within a system, governed by four fundamental laws. Energy can neither be created nor destroyed according to the First Law, also known as the law of energy conservation. The Second Law introduces the concept of entropy, a measure of disorder, and explains that natural processes tend to increase the overall entropy of the universe.

In the scope of our problem, these laws help determine the exergy or 'available energy' of the steam at different points in the process. Exergy is the maximum useful work possible during a process that brings a system into equilibrium with a heat reservoir, and the destruction of exergy is a consequence of inefficiencies and irreversibilities within a system.

The calculations provided in the problem, using thermodynamic properties from standard tables, show how engineers use these principles to predict the performance of thermal systems. For students, grasping the concepts of thermodynamics implies understanding how energy is transferred and transformed, and how irreversibilities due to friction, unrestrained expansions, and non-ideal heat transfer lead to the inevitable destruction of exergy.

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Most popular questions from this chapter

A natural gas-fired furnace in a textile plant is used to provide steam at \(130^{\circ} \mathrm{C}\). At times of high demand, the furnace supplies heat to the steam at a rate of \(30 \mathrm{MJ} / \mathrm{s}\). The plant also uses up to \(6 \mathrm{MW}\) of electrical power purchased from the local power company. The plant management is considering converting the existing process plant into a cogeneration plant to meet both their process-heat and power requirements. Your job is to come up with some designs. Designs based on a gas turbine or a steam turbine are to be considered. First decide whether a system based on a gas turbine or a steam turbine will best serve the purpose, considering the cost and the complexity. Then propose your design for the cogeneration plant complete with pressures and temperatures and the mass flow rates. Show that the proposed design meets the power and process-heat requirements of the plant.

Consider a 210-MW steam power plant that operates on a simple ideal Rankine cycle. Steam enters the turbine at \(10 \mathrm{MPa}\) and \(500^{\circ} \mathrm{C}\) and is cooled in the condenser at a pressure of \(10 \mathrm{kPa}\). Show the cycle on a \(T\) -s diagram with respect to saturation lines, and determine ( \(a\) ) the quality of the steam at the turbine exit, \((b)\) the thermal efficiency of the cycle, and \((c)\) the mass flow rate of the steam.

A large food-processing plant requires \(1.5 \mathrm{lbm} / \mathrm{s}\) of saturated or slightly superheated steam at 140 psia, which is extracted from the turbine of a cogeneration plant. The boiler generates steam at 800 psia and \(1000^{\circ} \mathrm{F}\) at a rate of \(10 \mathrm{lbm} / \mathrm{s}\) and the condenser pressure is 2 psia. Steam leaves the process heater as a saturated liquid. It is then mixed with the feedwater at the same pressure and this mixture is pumped to the boiler pressure. Assuming both the pumps and the turbine have isentropic efficiencies of 86 percent, determine \((a)\) the rate of heat transfer to the boiler and ( \(b\) ) the power output of the cogeneration plant.

Consider a coal-fired steam power plant that produces \(175 \mathrm{MW}\) of electric power. The power plant operates on a simple ideal Rankine cycle with turbine inlet conditions of \(7 \mathrm{MPa}\) and \(550^{\circ} \mathrm{C}\) and a condenser pressure of 15 kPa. The coal has a heating value (energy released when the fuel is burned) of \(29,300 \mathrm{kJ} / \mathrm{kg}\). Assuming that 85 percent of this energy is transferred to the steam in the boiler and that the electric generator has an efficiency of 96 percent, determine \((a)\) the overall plant efficiency (the ratio of net electric power output to the energy input as fuel) and \((b)\) the required rate of coal supply.

Why is the combined gas-steam cycle more efficient than either of the cycles operated alone?

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