1 Lec 8: Real gases, specific heats, internal energy, enthalpy.

Slides:



Advertisements
Similar presentations
Lecture 13 Use of the Air Tables.
Advertisements

CHAPTER 4: Energy Analysis of Closed Systems
Chapter 12 Thermodynamic Property Relations Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 7th edition by Yunus.
First Law of Thermodynamics
Department of Mechanical Engineering ME 322 – Mechanical Engineering Thermodynamics Lecture 19 Calculation of Entropy Changes.
State Postulate According to the State Postulate the number of intensive variable needed to specify all other intensive variables equals the number of.
Heat capacity and Specific Heat fixed P fixed V heat capacity per mole (or per gm…) i can correspond to either P or V.
Entropy Cengel & Boles, Chapter 6 ME 152.
Lec 19: Entropy changes, relative pressures and volumes, work
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.
Lec 7: Property tables, ideal and real gases
Chapter 4 Energy Analysis of Closed Systems Study Guide in PowerPoint to accompany Thermodynamics: An Engineering Approach, 5th edition by Yunus.
ES 202 Fluid and Thermal Systems Lecture 18: Making the Connection (1/23/2003)
Unit Three Quiz Solutions and Unit Four Goals Mechanical Engineering 370 Thermodynamics Larry Caretto February 25, 2003.
Thermodynamic Property Relations
Chapter 2 Simple Thermodynamics Systems
Specific Heat Thermodynamics Professor Lee Carkner Lecture 8.
ME1521 Properties of Pure Substances Reading: Cengel & Boles, Chapter 2.
Ideal Gas Law Physics 313 Professor Lee Carkner Lecture 10.
Instructor’s Visual Aids Heat Work and Energy. A First Course in Thermodynamics © 2001, F. A. Kulacki Chapter 2 Module 3 Slide 1 Equation of State for.
Chapter 5 Continued: More Topics in Classical Thermodynamics.
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Chapter 3 Phase Transitions and Chemical Reactions.
Calculating Entropy Change
THERMODYNAMIC PROPERTY RELATIONS
Chapter 6 Using Entropy.
CHAPTER 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
THERMODYNAMIC PROPERTY RELATIONS
Energy Analysis of Closed Systems Chapter 4. Recall that a closed system does not include mass transfer  Heat can get in or out  Work can get in or.
Thermodynamics I Inter - Bayamon Lecture 4 Thermodynamics I MECN 4201 Professor: Dr. Omar E. Meza Castillo
Entropy Rate Balance for Closed Systems
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:
1 The Ideal Gas. 2 Ideal gas equation of state Property tables provide very accurate information about the properties. It is desirable to have simple.
Chapter 4 Heat and the first law of thermodynamics
Thermodynamic Properties Property Table w Property Table -- from direct measurement w Equation of State w Equation of State -- any equations that relates.
Thermodynamics Properties of Fluids
ERT 206/4 THERMODYNAMICS SEM 1 (2012/2013) Dr. Hayder Kh. Q. Ali 1.
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.
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.
Entropy Property Relationships Chapter 7b. The T-ds relations Consider an internally reversible process occurring in a closed system.
Entropy Rate Balance for Closed Systems
1 Property Relationships Chapter 6. 2 Apply the differential form of the first law for a closed stationary system for an internally reversible process.
ACTIVITY AND ACTIVITY COEFFICIENT
1 Second Law of Thermodynamics - Entropy. 2 Introduction The second low often leads to expressions that involve inequalities.
Chapter 12 THERMODYNAMIC PROPERTY RELATIONS
Chapter 5 ENERGY ANALYSIS OF CLOSED SYSTEMS
MAXWELL’S THERMODYNAMIC RELATIONSHIPS AND THEIR APPLICATIONS
Unit Eight Quiz Solutions and Unit Nine Goals Mechanical Engineering 370 Thermodynamics Larry Caretto April 1, 2003.
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
CHAPTER 12 THERMODYNAMIC PROPERTY RELATIONS
Specific Heats Chapter 4
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 Three: Part Two
Chapter 12 THERMODYNAMIC PROPERTY RELATIONS
dU = dq + dw Now 1st Law becomes: dU = CvdT + PdV
Chapter Three: Part Two
THERMODYNAMICS SKMU 2113 LECTURER: PROFESSOR DR. MAZLAN ABDUL WAHID
Chapter 4 ENERGY ANALYSIS OF CLOSED SYSTEMS
Ch. 5: Applications Using Maxwell Relations & Measurable Properties
Chapter 3: Evaluating Properties
11 CHAPTER Thermodynamic Property Relations.
Heat Flow.
Presentation transcript:

1 Lec 8: Real gases, specific heats, internal energy, enthalpy

2 For next time: –Read: § 4-1 to 4-4 Outline: –Real gases (Compressibility factor) –Specific heats –Special relationships for ideal gases Important points: –How to manipulate the ideal gas law –Energy relationships to specific heats –How to evaluate properties of ideal gases

3 TEAMPLAY Under what conditions is it appropriate to apply the ideal gas equation of state?

4 Besides compressibility factor, we can also use more complex equations of state Van der Waals

5 Beattie-Bridgeman: where

6 Specific Heats Another set of properties that is a common combination of properties are the specific heats. They show up often. For simple compressible systems, these are:

7 Specific Heats c v is called the “constant volume” specific heat c p is called the “constant pressure” specific heat These names tell you how they are determined or measured. These names do not limit the applicability of them to either constant volume or constant pressure processes.

8 Specific Heats In general, the specific heats are functions of two variables for simple, compressible systems. However, we will show that for ideal gases, solids and liquids, they are functions of temperature alone

9 Specific Heats and Ideal Gases: Joule conducted some experiments where he found that the internal energy, u, was only a function of temperature, u = u(T). It was independent of P or v. This implies that c v is also only a function of temperature for an ideal gas:

10 We can start with du and integrate to get the change in u: Note that c v does change with temperature and cannot be automatically pulled from the integral.

11 Let’s look at enthalpy for an ideal gas: h = u + pv where pv can be replaced by RT because pv = RT. Therefore, h = u + RT => since u is only a function of T, R is a constant, then h is also only a function of T so h = h(T)

12 Similarly, for a change in enthalpy for ideal gases:

13 For an ideal gas, h = u + RT

14 Ratio of specific heats is given the symbol, k

15 Other relations with the ratio of specific heats which can be easily developed:

16 For monatomic gases,

17 For all other gases, c p is a function of temperature and it may be calculated from equations such as those in Table A-2 and A-2E in the appendices c v may be calculated from c p =c v +R. Next figure shows the temperature behavior….many specific heats go up with temperature.

18 Variation of Specific Heats with Temperature

19 Tabular specific heat data for c v, c p, and k are found in Tables A-2 and A-2E

20 Assumption of constant specific heats: when can you use it? where Either formulation for c p will be adequate because c p is fairly linear with T over a narrow temperature range. Take your choice.

21 Rule of thumb Specific heats for ideal gases may be considered to be constant when T 2 -T 1  200 K or 400 °R. (Note in many cases the temperature range can be significantly larger.)

22 Changes in enthalpy and internal energy can be calculated from tabular data: Frequently, we wish to know h 2 -h 1 or u 2 -u 1 and we do not want to go to the trouble to integrate where cp or cv is a third-degree polynomial in T, as shown in Tables A-2 and A-2E.

23 The integration is done for us in the ideal gas tables: Reference temperature is = 0 K and h = T ref = 0 K for ideal gas tables. Tables A-17 and A-17 are for air. Units are mass-based for both h and u.

24 Example Problem Calculate the change in enthalpy of air for a temperature rise from 300 to 800 K. a) assuming constant specific heats b) using the ideal gas tables

25 Solution For part a), we calculate the enthalpy difference using: Where,

26 Solution - Page 2 For constant specific heats:

27 Solution - Page 3 For variable specific heats, we’ll use the ideal gas air tables

28 Solution - Page 4 So for variable specific heats: Recall for constant specific heats, h = 520 kJ/kg, which is less than 0.5% difference.

29 Consider incompressible substances What’s an incompressible substance? –Liquid –Solid For incompressible substances v = constant dv = 0

30 Incompressible substances Express u = u(T,v) But dv = 0 for an incompressible substance, so We can take the derivative of u: 0

31 Incompressible substances The right hand side is only dependent on temperature. Thus, u = u(T) only for an incompressible substance. Recall that Thus:

32 Enthalpy of incompressible substances h = u + pv For an incompressible substance, v=const as before. If we hold P constant, then we can take (h/T) p and show:

33 Specific heats of incompressible substances: cpcp cvcv Bottom line: c p = c v = c for an incompressible substance.

34 Relationships for incompressible substances. du = c(T) dT

35 Relationships for incompressible substances. We can also show that:

36 Relationships for incompressible substances Now, if the temperature range is small enough, say up to about 200 K (400 °F), then c may be regarded as a constant, and u 2 - u 1 =c(T 2 - T 1 ) and h 2 - h 1 =c(T 2 - T 1 )+v(p 2 - p 1 )