ERT 206/4 THERMODYNAMICS SEM 1 (2012/2013) Dr. Hayder Kh. Q. Ali 1.

Slides:



Advertisements
Similar presentations
CHAPTER 4: Energy Analysis of Closed Systems
Advertisements

For a closed system consists of n moles, eq. (1.14) becomes: (2.1) This equation may be applied to a single-phase fluid in a closed system wherein no.
Chapter 12 Thermodynamic Property Relations Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 7th edition by Yunus.
1 Mathematical Methods Physics 313 Professor Lee Carkner Lecture 22.
Maxwell Relations Thermodynamics Professor Lee Carkner Lecture 23.
(Q and/or W) A closed system is one that does not exchange matter with its surroundings, although it may exchange energy. dn i = 0(i = 1, 2, …..)(1.1)
Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 19 Calculation of Entropy Changes.
EGR 334 Thermodynamics Chapter 6: Sections 1-5
Entropy Change Property diagrams (T-s and h-s diagrams) –From the definition of the entropy, it is known that  Q=TdS during a reversible process. –Hence.
Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 6 Thermodynamic Diagrams Phase Change Determination of Properties.
Lec 18: Isentropic processes, TdS relations, entropy changes
QUIZ 2 A refrigerator uses refrigerant-134a as the working fluid and operates on an ideal vapor-compression refrigeration cycle between 0.18 and 0.9 MPa.
1 Lec 8: Real gases, specific heats, internal energy, enthalpy.
Chapter 5 Simple Applications of Macroscopic Thermodynamics
Thermodynamic Property Relations
ME1521 Properties of Pure Substances Reading: Cengel & Boles, Chapter 2.
Observables. Molar System The ratio of two extensive variables is independent of the system size.  Denominator N as particle  Denominator N as mole.
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Chapter 3 PROPERTIES OF PURE SUBSTANCES
PTT 201/4 THERMODYNAMIC SEM 1 (2012/2013). Objectives Apply the second law of thermodynamics to processes. Define a new property called entropy to quantify.
Spontaneity and Equilibrium in Chemical Systems
Chapter 3 Phase Transitions and Chemical Reactions.
Eng. Samra Essalaimeh Philadelphia University 2nd Semester
THERMODYNAMIC PROPERTY RELATIONS
CHAPTER 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
THERMODYNAMIC PROPERTY RELATIONS
The Thermodynamic Potentials Four Fundamental Thermodynamic Potentials dU = TdS - pdV dH = TdS + Vdp dG = Vdp - SdT dA = -pdV - SdT The appropriate thermodynamic.
Entropy Chapter The important point is that since entropy is a property, the change in the entropy of a substance in going from one.
Thermodynamics I Inter - Bayamon Lecture 4 Thermodynamics I MECN 4201 Professor: Dr. Omar E. Meza Castillo
1 The Second Law of Thermodynamics (II). 2 The Fundamental Equation We have shown that: dU = dq + dw plus dw rev = -pdV and dq rev = TdS We may write:
33.1 Temperature Dependence of Gibbs’ Free Energy Methods of evaluating the temperature dependence of the Gibbs’ free energy can be developed by beginning.
1. (1.3) (1.8) (1.11) (1.14) Fundamental equations for homogeneous closed system consisting of 1 mole:
Thermodynamics Properties of Fluids
32.1 Pressure Dependence of Gibbs’ Free Energy Methods of evaluating the pressure dependence of the Gibbs’ free energy can be developed by beginning with.
Entropy Change Property diagrams (T-s and h-s diagrams) from the definition of the entropy, it is known that Q=TdS during a reversible.
Chapter 4: Applications of the First Law Different types of work: Configuration work: (reversible process) Dissipative work: (irreversible process) Adiabatic.
Lecture # 4 PROPERTIES OF PURE SUBSTANCES PURE SUBSTANCE.
Chapter 4 PROPERTIES OF PURE SUBSTANCES
Entropy Property Relationships Chapter 7b. The T-ds relations Consider an internally reversible process occurring in a closed system.
ERT 206/4 THERMODYNAMICS SEM 1 (2012/2013) Dr. Hayder Kh. Q. Ali 1.
Pressure – Volume – Temperature Relationship of Pure Fluids.
ACTIVITY AND ACTIVITY COEFFICIENT
Thermodynamics I Inter - Bayamon Lecture 7 Thermodynamics I MECN 4201 Professor: Dr. Omar E. Meza Castillo
Chapter 12 THERMODYNAMIC PROPERTY RELATIONS
Chapter 5 ENERGY ANALYSIS OF CLOSED SYSTEMS
Chapter 3 PROPERTIES OF PURE SUBSTANCES Dr. Kagan ERYURUK Copyright © The McGraw-Hill Companies, Inc. Permission required for reproduction or display.
MAXWELL’S THERMODYNAMIC RELATIONSHIPS AND THEIR APPLICATIONS
SOLUTION THERMODYNAMICS:
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Thermodynamics of Ideal Processes P M V Subbarao Professor Mechanical Engineering Department Entropy View of Theoretical Processes …..
Classical Thermodynamics of Solutions
공정 열역학 Chapter 3. Volumetric Properties of Pure Fluids
CHAPTER 12 THERMODYNAMIC PROPERTY RELATIONS
Exam #3 1. You should know from memory:
CHAPTER 3 ENERGY ANALYSIS OF CLOSED SYSTEMS
Prepared by: Lakhtartiya Amit A. Guided by: Mr. P. L. Koradiya
THERMODYNAMIC PROPERTY RELATIONS
SPECIFIC HEATS The specific heat is defined as the energy required to raise the temperature of a unit mass of a substance by one degree. In general, this.
CHAPTER 4: Energy Analysis of Closed Systems
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Chapter 12 THERMODYNAMIC PROPERTY RELATIONS
An Engineering Approach
PURE SUBSTANCE Pure substance: A substance that has a fixed chemical composition throughout. Air is a mixture of several gases, but it is considered to.
THERMODYNAMICS SKMU 2113 LECTURER: PROFESSOR DR. MAZLAN ABDUL WAHID
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Partial Derivatives and associated relations SMES1202 khkwek.
Thermodynamics Lecture Series
CHAPTER 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Chapter 3: Evaluating Properties
11 CHAPTER Thermodynamic Property Relations.
Presentation transcript:

ERT 206/4 THERMODYNAMICS SEM 1 (2012/2013) Dr. Hayder Kh. Q. Ali 1

2 Objectives Develop fundamental relations between commonly encountered thermodynamic properties and express the properties that cannot be measured directly in terms of easily measurable properties. Develop the Maxwell relations, which form the basis for many thermodynamic relations. Develop the Clapeyron equation and determine the enthalpy of vaporization from P, v, and T measurements alone. Develop general relations for c v, c p, du, dh, and ds that are valid for all pure substances.

3 A LITTLE MATH—PARTIAL DERIVATIVES AND ASSOCIATED RELATIONS The derivative of a function at a specified point represents the slope of the function at that point. The state postulate: The state of a simple, compressible substance is completely specified by any two independent, intensive properties. All other properties at that state can be expressed in terms of those two properties. The derivative of a function f(x) with respect to x represents the rate of change of f with x.

4

5 Partial Differentials Geometric representation of partial derivative (  z/  x) y. The variation of z(x, y) with x when y is held constant is called the partial derivative of z with respect to x, and it is expressed as The symbol  represents differential changes, just like the symbol d. They differ in that the symbol d represents the total differential change of a function and reflects the influence of all variables, whereas  represents the partial differential change due to the variation of a single variable. The changes indicated by d and  are identical for independent variables, but not for dependent variables.

6 Geometric representation of total derivative dz for a function z(x, y). This is the fundamental relation for the total differential of a dependent variable in terms of its partial derivatives with respect to the independent variables.

7

8

9 Partial Differential Relations The order of differentiation is immaterial for properties since they are continuous point functions and have exact differentials. Thus,

10 Reciprocity relation Cyclic relation Demonstration of the reciprocity relation for the function z + 2xy  3y 2 z = 0.

11

12 THE MAXWELL RELATIONS The equations that relate the partial derivatives of properties P, v, T, and s of a simple compressible system to each other are called the Maxwell relations. They are obtained from the four Gibbs equations by exploiting the exactness of the differentials of thermodynamic properties. Helmholtz function Gibbs function Maxwell relations Maxwell relations are extremely valuable in thermodynamics because they provide a means of determining the change in entropy, which cannot be measured directly, by simply measuring the changes in properties P, v, and T. These Maxwell relations are limited to simple compressible systems.

13

14 THE CLAPEYRON EQUATION

15 The slope of the saturation curve on a P-T diagram is constant at a constant T or P. The Clapeyron equation enables us to determine the enthalpy of vaporization h fg at a given temperature by simply measuring the slope of the saturation curve on a P-T diagram and the specific volume of saturated liquid and saturated vapor at the given temperature. General form of the Clapeyron equation when the subscripts 1 and 2 indicate the two phases. Clapeyron equation

16

17 At low pressures Treating vapor as an ideal gas The Clapeyron equation can be simplified for liquid–vapor and solid–vapor phase changes by utilizing some approximations. Substituting these equations into the Clapeyron equation Integrating between two saturation states The Clapeyron–Clausius equation can be used to determine the variation of saturation pressure with temperature. It can also be used in the solid–vapor region by replacing h fg by h ig (the enthalpy of sublimation) of the substance. Clapeyron–Clausius equation

18

19 GENERAL RELATIONS FOR du, dh, ds, c v, AND c p The state postulate established that the state of a simple compressible system is completely specified by two independent, intensive properties. Therefore, we should be able to calculate all the properties of a system such as internal energy, enthalpy, and entropy at any state once two independent, intensive properties are available. The calculation of these properties from measurable ones depends on the availability of simple and accurate relations between the two groups. In this section we develop general relations for changes in internal energy, enthalpy, and entropy in terms of pressure, specific volume, temperature, and specific heats alone. We also develop some general relations involving specific heats. The relations developed will enable us to determine the changes in these properties. The property values at specified states can be determined only after the selection of a reference state, the choice of which is quite arbitrary.

20 Internal Energy Changes

21 Internal Energy Changes

22 Enthalpy Changes The enthalpy to be a function of T and P, that is, h=h(T, P), and take its total differential:

23

24 Entropy Changes

25 Specific Heats c v and c p

26

27 Mayer relation

28 Mayer relation The volume expansivity (also called the coefficient of volumetric expansion) is a measure of the change in volume with temperature at constant pressure. Conclusions from Mayer relation: 1. The right hand side of the equation is always greater than or equal to zero. Therefore, we conclude that 2. The difference between c p and c v approaches zero as the absolute temperature approaches zero. 3. The two specific heats are identical for truly incompressible substances since v constant. The difference between the two specific heats is very small and is usually disregarded for substances that are nearly incompressible, such as liquids and solids.

29

30

31

32

33