THERMODYNAMICS. (For B.E./B.Tech Engineering Students) As per New Revised Syllabus of JNTU - Hydrabad, Kakinada & Anantapur

THERMODYNAMICS (For B.E./B.Tech Engineering Students) As per New Revised Syllabus of JNTU - Hydrabad, Kakinada & Anantapur Dr S. Ramachandran, M.E, Ph. D, Dr A. Anderson, M.E, Ph. D, Professor in Mechanical Engineering Department, SATHYABAMA UNIVERSITY, CHENNAI - 9 Dr Md Abid Ali, M.Tech, Ph. D, Professor in Mechanical Engineering Department, Ramachandra College of Engineering, Eluru, Andhra Pradesh-534007 AIRWALK PUBLICATIONS (Near All India Radio) 80, Karneeshwarar Koil Street Mylapore, Chennai - 600 004. Ph.: 466 909, 94440 8904 Email: aishram006@gmail.com, airwalk800@gmail.com www.airwalkbooks.com

th First Edition: 9 August 07 ISBN:978-93-84893-78- Price : ISBN : 978-93-84893-78- www.airwalkbooks.com

SYLLABUS II Year - I Semester- JNTU - KAKINADA THERMODYNAMICS UNIT I: Introduction: Basic Concepts: System, boundary, Surrounding, control volume, Universe, Types of Systems, Macroscopic and Microscopic viewpoints, Concept of Continuum, Thermodynamic Equilibrium, State, Property,Process, Cycle Reversibility Quasi static Process, Irreversible Process, Causes of Irreversibility Energy instate and in Transition, Types, Work and Heat, Point and Path function. Zeroth Law of Thermodynamics Concept of Temperature Principles of Thermometry Reference Points Const. Volume gas Thermometer Scales of Temperature, Ideal Gas Scale PMM I UNIT II: Joule s Experiments First law of Thermodynamics Corollaries First law applied to a Process applied to aflow system Steady Flow Energy Equation. PMM-I, throttling and free expansion processes deviations fromperfect gas model Vander waals equation of state compressibility charts variable specific heats gas tables. UNIT III: Limitations of the First Law Thermal Reservoir, Heat Engine, Heat pump, Parameters of performance, SecondLaw of Thermodynamics, Kelvin-Planck and Clausius Statements and their Equivalence / Corollaries, PMM ofsecond kind, Carnot s principle, Carnot cycle and its specialties, Thermodynamic scale of Temperature, ClausiusInequality, Entropy, Principle of Entropy Increase Energy Equation, Availability and Irreversibility Thermodynamic Potentials, Gibbs and Helmholtz Functions, Maxwell Relations Elementary Treatment of thethird Law of Thermodynamics. UNIT IV: Pure Substances, P-V-T- surfaces, T-S and h-s diagrams, Mollier Charts, Phase Transformations Triple point atcritical state properties during change of phase, Dryness Fraction Clausius Clapeyron Equation Propertytables. Mollier charts Various Thermodynamic processes and energy Transfer Steam Calorimetry. UNIT V: Mixtures of perfect Gases Mole Fraction, Mass friction Gravimetric and volumetric Analysis Dalton s Law ofpartial pressure, Avogadro s Laws of additive volumes Mole fraction, Volume fraction and partial pressure,equivalent Gas const. And Molecular Internal Energy, Enthalpy, sp. Heats and Entropy of Mixture of perfectgases and Vapour, Atmospheric air - PsychrometricProperties Dry bulb Temperature, Wet Bulb Temperature,Dew point Temperature, Thermodynamic Wet Bulb Temperature, Specific Humidity, Relative Humidity, saturated Air, Vapour pressure, Degree of saturation Adiabatic Saturation, Carrier s Equation Psychrometricchart. UNIT - VI: Power Cycles: Otto, Diesel, Dual Combustion cycles, Sterling Cycle, Atkinson Cycle, Ericcson Cycle, LenoirCycle Description and representation on P V and T-S diagram, Thermal Efficiency, Mean Effective Pressureson Air standard basis comparison of Cycles. Refrigeration Cycles: Brayton and Rankine cycles Performance Evaluation combined cycles, Bell- Colemancycle, Vapour compression cycle-performance Evaluation.

II Year - I Semester- JNTU - HYDRABAD ME304ES: THERMODYNAMICS B.Tech. II Year I Sem. UNIT I Introduction: Basic Concepts: System, Control Volume, Surrounding, Boundaries, Universe, Types of Systems, Macroscopic and Microscopic viewpoints, Concept of Continuum, Thermodynamic Equilibrium, State, Property, Process, Exact & Inexact Differentials, Cycle Reversibility Quasi static Process, Irreversible Process, Causes of Irreversibility Energy in State and in Transition, Types, Displacement& Other forms of Work, Heat, Point and Path functions, Zeroth Law of Thermodynamics Concept of Temperature Principles of Thermometry Reference Points Const. Volume gas Thermometer Scales of Temperature, Ideal Gas Scale UNIT - II PMM I - Joule s Experiments First law of Thermodynamics Corollaries First law applied to a Process applied to a flow system Steady Flow Energy Equation. Limitations of the First Law Thermal Reservoir, Heat Engine, Heat pump, Parameters of performance, Second Law of Thermodynamics, Kelvin-Planck and Clausius Statements and their Equivalence / Corollaries, PMM of Second kind, Carnot s principle, Carnot cycle and its specialties, Thermodynamic scale of Temperature, Clausius Inequality, Entropy, Principle of Entropy Increase Energy Equation, Availability and Irreversibility Thermodynamic Potentials, Gibbs and Helmholtz Functions, Maxwell Relations Elementary Treatment of the Third Law of Thermodynamics UNIT III Pure Substances, p-v-t- surfaces, T-S and h-s diagrams, Mollier Charts, Phase Transformations Triple point at critical state properties during change of phase, Dryness Fraction Clausius Clapeyron Equation Property tables. Mollier charts Various Thermodynamic processes and energy Transfer Steam Calorimetry. Perfect Gas Laws Equation of State, specific and Universal Gas constants various Nonflow processes, properties, end states, Heat and Work Transfer, changes in Internal Energy Throttling and Free Expansion Processes Flow processes UNIT - IV Deviations from perfect Gas Model Vader Waals Equation of State Compressibility charts variable specific Heats Gas Tables Mixtures of perfect Gases Mole Fraction, Mass friction Gravimetric and volumetric Analysis Dalton s Law of partial pressure, Avogadro s Laws of additive volumes Mole fraction, Volume fraction and partial pressure, Equivalent Gas const. And Molecular Internal Energy, Enthalpy, sp. Heats and Entropy of Mixture of perfect Gases and Vapour, Atmospheric air - Psychrometric Properties Dry bulb Temperature, Wet Bulb Temperature, Dew point Temperature, Thermodynamic Wet Bulb Temperature, Specific Humidity, Relative Humidity, saturated Air, Vapour pressure, Degree of saturation Adiabatic Saturation, Carrier s Equation Psychrometric chart. UNIT - V Power Cycles: Otto, Diesel, Dual Combustion cycles, Sterling Cycle, Atkinson Cycle, Ericsson Cycle, Lenoir Cycle Description and representation on P V and T-S diagram, Thermal Efficiency, Mean Effective Pressures on Air standard basis comparison of Cycles. Refrigeration Cycles: Brayton and Rankine cycles Performance Evaluation combined cycles, Bell-Coleman cycle, Vapour compression cycle-performance Evaluation.

JAWAHARLAL NEHRU TECHNOLOGICAL UNIVERSITY ANANTAPUR B.Tech. II - I Sem. (3A0330) THERMODYNAMICS UNIT I BASIC CONCEPTS: Macroscopic and Microscopic Approaches, Thermodynamic System, State, Property, Process and Cycle, Quasi Static Process, Thermodynamic Equilibrium, Quasi-static Process, Zeroth Law of Thermodynamics, WORK & HEAT TRANSFER: Work transfer, types of work transfers, Point and Path Functions, Heattransfer, Comparison of Work and Heat transfers. UNIT II FIRST LAW OF THERMODYNAMICS: First Law applied to a process and a cycle, Energy - a property, Forms and transformation of Energy, Internal Energy and Enthalpy, PMM I. FLOW SYSTEMS: Control Volume, Steady Flow Process, Mass balance and Energy Balance, Applications of Steady Flow Processes. UNIT III Second Law of Thermodynamics: Heat Engine, Statements of Second law and their equivalence, Refrigeration and Heat Pump, Reversibility and Irreversibility, Carnot cycle and Carnot s Theorem, Thermodynamic Temperature Scale, Efficiency of Heat Engine, PMM II Entropy: Clausius Theorem, Entropy as a property, T-s Plot, Clausius Inequality, Principle of Entropy Increase and its applications. Available Energy, Quality of Energy, definitions of Dead state, Availability. UNIT IV Pure Substances: P-v, P-T, T-s diagrams of Pure Substances, Mollier Diagram, Dryness Fraction, Use ofsteam Tables for Thermodynamic PropertiesThermodynamic Relations: Maxwell s equations, TDS equations, Joule-Kelvin Effect, Clausiusclapeyronequation. UNIT V Properties of Gases and Gas Mixtures: Ideal Gas, Equation of State, Avogadro s Law, Internal Energy and Enthalpy of Ideal Gas, Entropy Change of Ideal Gas, Mixture of Gases- Dalton s Law of Partial Pressure, Specific Heats, Internal Energy and Enthalpy of Gas Mixtures Gas Power Cycles: Carnot Cycle, Sterling Cycle, Ericson Cycle, Otto Cycle, Diesel Cycle, Dual Cycle,their applications, comparison of Otto, Diesel and Dual cycles, Second Law Analysis of Gas PowerCycles

Contents C. Contents. Basic Concepts and Zeroth Law of Thermodynamics. Introduction..... Role of Thermodynamics in Engineering and Science.....3 Applications of Thermodynamics.....4 Founders of Thermodynamics....3.5 Basic Concepts....4.5. Units and Dimensions....4.5. Mass....4.5.3 Force....4.5.4 Pressure....5.5.5 Temperature....6.5.6 Specific Volume and Density....6.5.7 Energy....7.5.8 Power....7.5.9 Dimensional Homogeneity....7.6 Macroscopic And Microscopic Viewpoints....8.6. Macroscopic viewpoint....8.6. Microscopic viewpoint....8.7 Concept of Continuum....9.8 Thermodynamic Systems....0.8. Types of system....0.9 Closed System....0.0 Open System..... Isolated System..... Homogeneous and Heterogeneous Systems...... Pure substance...... State postulate.....3 Property....

C. Thermodynamics - www.airwalkbooks.com.4 State, Path and Process....3.5 Cycle....4.6 Thermodynamic Equilibrium....5.7 Quasi-static (or) Quasi equilibrium Process....5.8 Path Function and Point Function....7.9 Zeroth Law of Thermodynamics....8.9. Equality of temperature....8.0 Measurement of Temperature....8.0. Thermometry....9.0. Applications of thermometry....9. Thermometric Property....9.. Reference points....9. Comparison of Thermometer.....3 Equation of State.....4 Ideal Gas.....5 Ideal Gas Temperature Scale....4.6 Celsius Temperature Scale....5.6. Contradiction in kelvin scale....5.7 Gas Thermometers....6.8 Thermocouple....7.9 Resistance Thermometers....8.30 Energy....3.30. Different forms of energy....3.3 Work....3.3 Work Transfer - A Path Function....33.33 Different Modes of Work....34.33. Electrical work....34.33. Shaft Work....35.33.3 Spring Work....36.33.4 Paddle wheel work (or) Stirring work....38.33.5 Flow Work....38.33.6 Workdone on Elastic solid bars...

Contents C.3.39.33.7 Work Associated with the stretching of a Liquid Film....39.33.8 Workdone per unit volume on a magnetic material....40.34 Free Expansion Work....4.35 Heat....4.35. Heat Transfer A Path Function....44.36 Heat Capacity....45.37 Reversible and Irreversible Process....45. First Law of Thermodynamics. First Law of Thermodynamics..... Joules Experiment.....3 Perpetual Motion of Machine of First Kind....3.4 First Law for a Closed System Undergoing Change of State....3.4. Internal Energy....3.4. Energy - A property of the system....4.5 Specific Heat Capacities....8.5. Specific heat....8.5. Latent heat....9.5.3 Specific heat at constant volume....9.5.4 Enthalpy....0.5.5 Specific heat at constant pressure....0.6 Thermodynamic Processes.....7 Application of First Law to Non-flow Process (or) Closed System.....7. Constant Volume Process (or) isochoric Process.....7. Constant Pressure Process (or) isobaric Process....5

Contents C.5 3.6. Heat Pump... 3.8 3.7 Coefficient of Performance - Cop... 3.9 3.8 Equivalence of The Two Statements... 3.0 3.9 Perpetual-motion Machines... 3. 3.0 Reversibility and Irreversibility... 3. 3.0. Reversibilities... 3. 3.0. Irreversibilities... 3. 3.0.. Types of Irreversibility... 3.4 3. Carnot Cycle... 3.4 3. Reversed Carnot Cycle... 3. 3.3 The Carnot Principles (or) Carnot Theorem... 3. 3.4 Absolute Thermodynamic Temperature Scale... 3.4 3.5 Efficiency of The Carnot Heat Engine... 3.7 3.6 The Cop of The Carnot Refrigerator and Heat Pump... 3.8 3.6. Reversed Heat engines... 3.30 3.7 Corollaries of Carnot s Theorem... 3.33 3.8 Equality of Thermodynamic Temperature Scale With Perfect Gas Scale... 3.34 3.8. Absolute zero... 3.35 3.9 Clausius Inequality... 3.36 3.0 Concept of Entropy... 3.4 3.0. Characteristics of entropy... 3.44 3.0. Entropy Transfer with Heat Flow... 3.46 3. Principle of Increase of Entropy... 3.47 3. Property Diagrams Involving Entropy... 3.49 3.3 What Is Entropy?... 3.50 3.4 Entropy Change of Ideal Gas... 3.5 3.5 Entropy Balance... 3.68 3.6 Entropy Generation... 3.70 3.7 Third Law of Thermodynamics... 3.00

C.6 Thermodynamics - www.airwalkbooks.com 3.7. Fowler Guggenheim statement of the third law... 3.00 3.7. Nernst-Simon statement of the third law... 3.0 4. Exergy 4. Introduction... 4. 4.. High grade energy... 4. 4.. Low grade energy... 4. 4..3 Available energy... 4. 4..4 Unavailable energy... 4. 4. Law of Degradation of Energy... 4. 4.3 Availability - Exergy - Work Potential of Energy... 4. 4.4 Useful Work... 4.3 4.4. Actual work... 4.3 4.4. Surrounding work... 4.3 4.4.3 Reversible work... 4.4 4.4.4 The Rate of Irreversibility of a Heat Engine... 4.4 4.5 Dead State... 4.5 4.6 Exergy Analysis... 4.6 4.7 Available Energy Referred to a Cycle... 4.6 4.8 Availability of a Closed System... 4.8 4.8. Availability function of a closed system with reference to dead state... 4.0 4.8. Maximum useful work... 4. 4.9 Maximum Work in a Reversible Process... 4. 4.0 Availability of An Open System (Steady Flow Process)... 4. 4.0. Availability function of a open system with reference to dead state... 4.3 4. Irreversibility... 4.4 4.. Gouy-Stodola theorem... 4.5

Contents C.7 4. Effectiveness... 4.5 4.3 Exergy Destruction... 4.6 4.3. Important Hints about Availability... 4.6 5. Properties of Pure Substance 5. Properties of Pure Substances... 5. 5. Thermodynamic Properties of Pure Substances in Solid, Liquid and Vapour Phases... 5. 5.3 Saturated Vapour and Superheated Vapour... 5. 5.4 Saturation Temperature and Saturation Pressure... 5.4 5.5 Property Diagrams For Phase-change Processes... 5.4 5.5. T-v Diagram... 5.4 5.5. P v Diagram... 5.7 5.5.3 P-T Diagram... 5.9 5.5.4 T-s Diagram... 5.0 5.5.5 h s Diagram or Mollier Diagram... 5. 5.5.6 T-h diagram... 5.4 5.6 P-v-T Surfaces... 5.5 5.7 Thermodynamic Properties of Steam... 5.7 5.7. Property Tables... 5.7 5.7. Saturated Liquid and Saturated Vapour States... 5.7 5.7.3 Saturated Liquid-Vapour Mixture... 5.8 5.7.4 Superheated Vapour... 5.8 5.7.5 Thermodynamic properties of steam... 5.9 5.8 Calculation of Workdone and Heat Transfer in Non-flow and Flow Processes... 5.37 5.8. Constant volume process... 5.37 5.8.. Constant pressure process... 5.4 5.8.3 Isothermal process and hyperbolic process... 5.44 5.8.4 Isentropic process... 5.46

C.8 Thermodynamics - www.airwalkbooks.com 5.8.5 Throttling process... 5.5 5.8.5. Throttling Calorimeter... 5.5 5.8.5. Separating and Throttling Calorimeter... 5.56 5.9 Standard Rankine Cycle... 5.66 5.9. The Ideal Cycle for Vapour Power Cycles... 5.66 5.9. Efficiency of Standard Rankine Cycle... 5.68 5.0 Rankine Cycle - Reheating Cycle... 5.75 5.0. Advantages (or) Effects of Re-heating... 5.77 5. Re-generation: Regenerative Cycle (Bleeding Cycle)... 5.88 5.. Advantages of Regenerative cycle... 5.9 5. Binary Vapour Cycle and Combined Cycle... 5.04 6. Behaviour of Ideal and Real Gases 6. Gas Mixtures... 6. 6. Composition of a Gas Mixtures... 6. 6.3 Relationship Among Properties... 6. 6.4 Mole Fraction... 6. 6.5 Mass Fraction... 6. 6.6 Relationship Between Mass and Mole Fractions... 6.3 6.7 Properties of Ideal Gas... 6.4 6.7. Equation of state... 6.4 6.8 Avogadro s Law... 6.5 6.9 Universal Gas Constant and Characteristic Gas Constant 6.6 6.0 Partial Pressure... 6.7 6. Partial Volume... 6.7 6. Dalton s Law of Partial Pressure... 6.8 6.3 Amagat s Law of Partial Volume... 6.0 6.4 Properties of Gas Mixtures... 6.0 6.5 Molar Mass of a Gas Mixture... 6.0 6.6 Gas Mixture Constants... 6. 6.7 Gibbs Dalton s Law... 6.3 6.8 Properties of Real Gas... 6.40 6.9 Vander Waal s Equation of State... 6.40 6.9. Berthelot equation of state... 6.40

Contents C.9 6.9. Dieteric equation of state... 6.40 6.9.3 Redlich-Kwong equation of state... 6.4 6.0 Compressibility Factor... 6.4 6.0. Virial expansions... 6.4 6.0. Compressibility Chart... 6.43 6. Phase Change Process... 6.46 6. Kay s Rule... 6.46 6.3 Comparison Between Ideal and Real Gases... 6.49 7. Thermodynamic Relations 7. Introduction... 7. 7. Fundamental Mathematical Theorems... 7. 7.3 Maxwell s Equations... 7.3 7.4 Tds Relations... 7.5 7.4. Entropy Equations... 7.5 7.4.. First Tds equation... 7.5 7.4.. Second Tds equations... 7.6 7.5 Equations For Internal Energy, Enthalpy and Entropy. 7.7 7.5. Internal energy equation... 7.7 7.5. Enthalpy equation... 7.7 7.5.3 Entropy equations... 7.8 7.6 Specific Heat Relations... 7.8 7.6. Specific heat at constant volume... 7.8 7.6. Specific heat at constant pressure... 7.8 7.6.3 Specific heats difference... 7.8 7.6.4 Ratio of specific heats... 7. 7.7 The Clapeyron Equation (Clausius Clapeyron Equation) 7. 7.8 Throttling Process... 7.4 7.9 Joule Kelvin Effect and Inversion Curves... 7.4 7.0 Co-efficient of Volume Expansion... 7.8 7. Isothermal Compressibility... 7.8

C.0 Thermodynamics - www.airwalkbooks.com 8. Psychrometry 8. Psychrometry... 8. 8.. Uses of Psychrometry... 8. 8. Psychrometric Parameters... 8. 8.. Measurement of Parameters... 8. 8.3 Psychrometric Properties... 8. 8.3. Dalton s Law... 8. 8.3. Partial Pressure... 8. 8.3.3 Specific humidity (or) Humidity ratio (or) Moisture content:... 8.3 8.3.4 Degree of saturation (or) Percentage humidity 8.4 8.3.5 Relative humidity (RH),... 8.4 8.4 Property Calculations of Air Vapour Mixtures (Using Formula)... 8.5 8.5 Psychrometric Charts... 8.9 8.6 Calculation of Parameters Using Psychrometric Charts. 8. 8.6. To Read Wet Bulb temperature... 8. 8.6. To Read Dew Point Temperature... 8. 8.6.3 To Read Specific Humidity... 8.3 8.6.4 To Read Enthalpy... 8.3 8.7 Psychrometric Process... 8.5 8.7. Sensible Heating Process... 8.6 8.7.. Sensible Cooling Process... 8.36 8.7.3. Cooling and Dehumidification ( t decreases and decreases)... 8.39 8.7.4 Cooling and Humidification: ( t decreases and increases)... 8.4 8.7.5 Heating and Dehumidification... 8.4 8.7.6 Heating and Humidification... 8.4 8.7.7 Adiabatic [No heat transfer] Saturation Process... 8.43 8.7.8. Adiabatic Mixing of Two Air Streams... 8.48

Contents C. 9. Gas Power Cycles 9. Gas Power Cycles... 9. 9. Different Types of Air Standard Cycles... 9. 9.. Air Standard Efficiency... 9. 9.3 Carnot Cycle... 9.3 9.4 Stirling Cycle... 9.5 9.5 Ericsson Cycle... 9.8 9.6 Otto Cycle (or) Constant Volume Cycle... 9.9 9.7 Diesel Cycle or Constant Pressure Cycle... 9.4 9.8 Dual Combustion Cycle... 9.47 9.9 Comparison of Otto, Diesel And Dual Combustion Cycles 9.65 9.0 Atkinson Cycle... 9.67 9. Lenoir Cycle... 9.70 0. Brayton Cycles and Refrigeration Cycles 0. Brayton Cycle - Ideal Gas Turbine Cycle... 0. 0.. Gas turbine Open cycle... 0. 0.. Gas turbine Closed cycle... 0. 0. Optimum Pressure Ratio for Maximum Specific Work Output 0.5 0.3 Bell-coleman Cycle... 0. 0.4 Vapour Compression Refrigeration... 0.4 0.4. Different Conditions of the Vapour... 0.6 0.5 Performance Evaluation - Factors Affecting Performance Of A Vapour Compression System... 0.34 0.5. Calculations in a vapour compression refrigeration system.... 0.35

Chapter Basic Concepts and Zeroth Law of Thermodynamics. INTRODUCTION Thermodynamics can be defined as the science which deals with the transformation of energy and its effects on the properties of the substance. The word Thermodynamics originates from two Greek words, therme (heat) and dynamis (motion or power). Thermodynamics can also be called as the science of 3E s i.e., Equilibrium, Energy and Entropy. Thermodynamics is a branch of Science that deals with the relationship among heat, work and properties of system which are in equilibrium with one another. One of the most fundamental laws of nature is the conservation of energy principle. It states that during an interaction, energy can change from one form to another but the total amount of energy remains constant. i.e., Energy can neither be created nor be destroyed, but it can be transformed from one form to another. For example,. A ball falling from a tower picks speed as a result of its potential energy being converted to kinetic energy.. A person eating more and working less i.e., a person who has a greater energy input (food) than energy output (exercise) will gain weight (store energy in the form of fat) The first law of thermodynamics is based on the conservation of energy principle. The second law of thermodynamics reveals that energy has quality as well as quantity and actual processes occur in the direction of decreasing quality of energy. For example, a cup of hot coffee in a room eventually cools, but a cup of cool coffee never gets hot by itself. The first and second laws of thermodynamics emerged simultaneously in the 850s, by the works of James Prescott Joule, William Rankine, Rudolph Clausius and Lord Kelvin.

. Thermodynamics - www.airwalkpublications.com. ROLE OF THERMODYNAMICS IN ENGINEERING AND SCIENCE Thermodynamics plays a vital role in the field of Engineering and Science. They are explained as follows. Thermodynamics is very important in the design, analysis and development of Engineering systems such as the power-producing systems like engines, turbines etc. and the power-consuming systems like compressor, pumps, etc. The working principle of many scientific devices like thermometer, thermistor, thermostat etc... involves thermodynamics. Good understanding and careful applications of the fundamentals of thermodynamics leads to improved design, increased efficiency, optimum operating conditions and decreased levels of environmental pollution etc..3 APPLICATIONS OF THERMODYNAMICS Thermodynamic principles are applied in various fields of Engineering and Technology. Some of the fields are (i) Internal combustion engine (ii) Gas turbines (iii) Air conditioner & Refrigerator (iv) Compressor (v) Steam and Nuclear power plants (vi) Rockets (vii) Jet engines etc. Applications of thermodynamics are found in various aspects of life eg: A commonly encountered thermodynamics application is, the human heart, which is constantly pumping blood to all parts of the body. The movement of blood and various energy conversions generates heat, within the body. (normally called as body heat). The generated heat is constantly rejected to the environment and the process is called as metabolic heat rejection. However, this heat rejection can be controlled by adjusting our clothing to the environment conditions. Other application of thermodynamics involves increasing the heat transfer rate like exhaust fan in a house, cooling fans in the computer CPU and fins provided on the engine cylinders etc.

Basic Concepts and Zeroth Law of Thermodynamics.3.4 FOUNDERS OF THERMODYNAMICS Founders. Antoine Laurent Lavoisier (743-794). Nicolas Leonard Sadi Carnot (796-83) 3. James Prescott Joule (88-889) 4. William Thompson (also called as Lord Kelvin) (89-907) 5. Rudolph J. Clausius (8-888) Contribution - Father of Modern Chemistry - Developed combustion process - Also, proposed the name for oxygen (which was discovered by Joseph priestely) and mentioned its importance in the combustion process. - Father of Thermodynamics - Developed carnot cycle - Established the basic principles governing the conversion of heat to work, that led to the fundamental laws of thermodynamics. - Established heat as a form of energy which led to the dismissal of calorific theory of heat. - Developed First law of Thermodynamics with experimental proof that supports the heat, is also an energy. - Absolute temperature scale is named after him. - Developed Thermodynamic temperature scale. - Along with joule, he expounded Joule-Kelvin effect. - Developed Second Law of Thermodynamics - Also, led to the founding of the Thermodynamic property called entropy.

.4 Thermodynamics - www.airwalkpublications.com.5 BASIC CONCEPTS Some important basic concepts of thermodynamics are discussed in this Chapter..5. Units and Dimensions Nowadays, the SI (System International) system of units has been used. Any physical quantity can be characterised by dimensions. The arbitrary magnitudes assigned to the dimensions are called Units. Some basic dimensions such as mass m, length L, time t and temperature T are selected as primary (or) fundamental dimensions, while others such as velocity V, energy E, and volume V are expressed in terms of primary dimensions and are called secondary dimensions (or) derived dimensions. A number of unit systems have been developed over the years. But nowadays, the SI (System International) system of units are widely used. The SI is simple and logical system. Some fundamental dimensions and their units in SI are given in the following table. Dimensions Unit Symbol Length metre m Mass kilogram kg Time second s Temperature Kelvin K Electric current Ampere A Amount of light Candela cd Amount of matter mole mol.5. Mass m It is quantity of matter. Its unit is kg..5.3 Force In SI, the unit for force is derived from Newton s second law. i.e., Force Mass Acceleration F m a In SI, the force unit is the Newton N and it is defined as the force required to accelerate a mass of kg at a rate of m/s. i.e., N kg m/s

Basic Concepts and Zeroth Law of Thermodynamics.5 The weight of a body W is the force with which the body is attracted to the centre of the earth. It is the product of its mass m and the local gravitational acceleration g, i.e., W mg where g 9.80665 9.8 m/s at sea level. The mass m of a body will remain same regardless of its location in the universe. Its weight, however, will change with a change in gravitational acceleration. A body will weigh less on top of a mountain since g decreases with altitude. At sea level, a mass of kg will weigh 9.807 N..5.4 Pressure Pressure is the normal force exerted A by a system against unit area of the bounding surface. F If A is a small area and A is the n smallest area from the concept of SYSTEM continuum, and F n is the component of force normal to A, the pressure P at a point Definition of pressure on the wall is defined as Fig.. F n P lim A A A The pressure P at a point in a fluid in equilibrium is the same in all directions. The unit for pressure in the SI system is the Pascal Pa, which is the force of N acting on an area of m. Pascal Pa N/m The unit of pascal is very small. Hence, very often, kilo-pascal (kpa) (or) mega-pascal (MPa) is used. Sometime bar and standard atmosphere are used which are not within the SI system of units. bar 0 5 Pa 00 kpa 0. M Pa and Standard atmosphere atm 0.35 kpa.035 bar Most of the instruments indicate pressure relative to the atmospheric pressure where as the pressure of a system is its pressure above zero (or) relative to a perfect vacuum.

.6 Thermodynamics - www.airwalkpublications.com Absolute pressure The pressure relative to the atmosphere is called gauge pressure. The pressure relative to a perfect vacuum is called absolute pressure. Gauge pressure Atmospheric pressure The SI unit prefixes are used in all branches of engineering. Some standard prefixes in SI units for Mechanical Engineering branch are given in the table. Multiple Prefix 0 Tera, T 0 9 Giga, G 0 6 Mega, M 0 3 Kilo, k 0 3 milli, m 0 6 micro, 0 9 nano, n 0 pico, p.5.5 Temperature It is defined as the degree of intensity of heat or measure of hotness or coldness of a body. Temperature - Intensive property - C or K (Centigrade or Kelvin). 30 C 30 73 303 K Normally, t is for C and T is for K..5.6 Specific Volume and Density Volume V is the space occupied by a substance and is measured in m 3. The specific volume v of a substance is defined as the volume per unit mass and is measured in m 3 /kg. From the concept of continuum, the specific volume at a point is defined as v lim V V where V is the smallest volume for which the system can be considered as continuum. V m

Basic Concepts and Zeroth Law of Thermodynamics.7 Specific volume: v Volume Total volume V in m 3 Specific volume Volume V mass m v Its unit is m 3 /kg Density : It is the mass of the substance per unit volume. Its unit is kg/m 3. Density is the mass per unit volume of a substance and is given in kg/m 3. m V.5.7 Energy Work, which is a form of energy, can simply be defined as force times distance. Therefore, it has the unit newton-meter (N-m) which is called a Joule J. i.e., J N m A more common unit for energy in SI is the kilojoule kj 0 3 J. The energy per unit mass is the specific energy and its unit is J/kg. In the metric system, the amount of energy needed to raise the temperature of kg of water at 5 C by C is defined as kilocalorie (kcal), and kcal 4.87 kj..5.8 Power The rate of energy transfer (or) storage is called power. The unit of power is Watts (W), kilowatts kw (or) MegaWatts (MW). W J/s Nm/s; kw 000 W.5.9 Dimensional Homogeneity In engineering, all equations must be dimensionally homogeneous. i.e., every term in an equation must have the same unit. Analyse the following equation, E 35 kj 8 kj/kg where E is the total energy in kj. Since the two terms on the right hand side do not have the same units, they can not be added to obtain the total energy. Multiplying the last term 8 kj/kg m kg by mass will eliminate the

.8 Thermodynamics - www.airwalkpublications.com kilograms in denominator, and the whole equation will become dimensionally homogeneous i.e., every term in the equation will have the same unit. i.e., E 35 kj 8 m kj.6 MACROSCOPIC AND MICROSCOPIC VIEWPOINTS Normally, a substance consists of a large number of particles called molecules and the properties of substance naturally depend on the behaviour of these particles. There are two points of view from which the behaviour of particles can be studied. They are Viewpoints Macroscopic Viewpoint (or) Classical Thermodynamics Microscopic Viewpoint (or) statistical Thermodynamics.6. Macroscopic viewpoint In this point of view, a certain amount of matter is considered, neglecting the events occurring at the molecular level. It does not require a knowledge on the behaviour of individual particles. It provides a direct and easy way to the solution of engineering. In general, macroscopic point of view is just like, inventing a device or using a instrument, to measure the quantities directly, instead of finding it out through calculation, derivation and formulas. eg: Pressure gauge is used to measure pressure directly without calculating force on a given unit area. Likewise, temperature can also be measured using thermometer. However, macroscopic point of view is limited to those effects that can be perceived by human senses..6. Microscopic viewpoint In this point of view, behaviour of each molecule has to be studied, to find out the behaviour of the entire substance. Each molecule at a given instant has certain position, velocity and energy, for each molecule these changes frequently as a result of collisions. And also, these effects cannot be perceived by human senses. In general, microscopic point of view requires large number of data and equations to find out the quantities through calculation and derivation.

Basic Concepts and Zeroth Law of Thermodynamics.9 eg: Impulse, Enthalpy, Entropy, Gibbs function, Helmhotz function etc. Macroscopic viewpoint. It is also called as classical thermodynamics.. Behaviour of each molecule need not to be determined. 3. Molecular effects can be perceived by human senses. 4. Classical thermodynamics, however can be derived from statistical thermodynamics. Microscopic viewpoint It is also called as statistical thermodynamics. Behaviour of each molecule need to be determined. Molecular effects cannot be perceived by human senses. Statistical thermodynamics cannot be determined using classical thermodynamics. 5. eg: Pressure, Temperature eg: Enthalpy, Entropy.7 CONCEPT OF CONTINUUM Generally, matter is made up of atoms & these atoms are widely spaced in the gas phase. From the macroscopic viewpoint, behaviour of individual molecules can be disregarded and the matter with widely spaced atoms can be treated as continuous because a large no. of molecules can accommodate even in an extremely small volume of atom. This view of continuous, homogeneous matter with no holes is called as continuum. The continuum idealization allow us to treat properties as a point function and to assume that the properties vary continuously in space with no jump discontinuities. Concept of continuum can be verified by the dimensionless parameter known as knudsen number k n. k n Mean free path of the molecules Characteristic Length of the system L If knudsen number, k n 0.0, then the concept of continuum holds good. i.e., the continuum model can be applicable as long as the characteristic length of the system is much larger than the mean free path of the molecules. At very high vacuums or high elevations, the mean free path becomes large, for such cases rarefield gas flow theory should be used and the impact of individual molecules should be considered. But in most engineering applications, however the continuum is valid and convenient & goes hand in hand with the macroscopic point of view.

Surro undings.0 Thermodynamics - www.airwalkpublications.com.8 THERMODYNAMIC SYSTEMS Thermodynamic system is known as a space or constrained area upon which our attention is concentrated on. It is the region to be studied. The system has boundary (or) boundary line. Anything outside the boundary is called surroundings. In other words, the system and surroundings are separated by Surroundings undary. (Boundary may be real or imaginary)..8. Types of system The systems are classified into:. Closed system,. Open system, 3. Isolated system. System Surroundings Fig.. Boundary System may be considered to be closed (or) open, depending on whether a fixed mass (or) a fixed volume in space is chosen for study. b o.9 CLOSED SYSTEM A closed system, also known as a control mass, consists of a fixed amount of mass and no mass can cross its boundary. i.e., no mass can enter (or) leave a closed system as shown in Fig..3 But energy, in the form of heat (or) work, can cross the boundary. And the volume of a closed system does not CLOSED SYSTEM m = constant Mass NO energy YES Mass cannot cross the boundaries of a closed system, but energy can. Fig..3 Closed system (or Non flow system) Open system(or) Steady flow system Energy in System boundary Energy out L.P. air in System System (Air compressor) HP air out Work in No m ass transfer Fig..4 Fig..5 Work in

Basic Concepts and Zeroth Law of Thermodynamics. have to be fixed. Energy is transferred from the surroundings into the system and from the system to the surroundings. But there is no mass transfer in closed system. Eg. Piston and cylinder without valves Fig..4. Control surface.0 OPEN SYSTEM mass YES An open system is a properly selected region in space. It usually encloses CONTROL a device that involves mass flow. A large VOLUME number of engineering problems involve mass flow in and out of a system and, energy YES therefore, are modeled as control volumes. In general, any arbitrary region in space can be selected as a control volume. The boundaries of a control volume are called a Fig..6 control surface as shown in Fig..6 and they can be real (or) imaginary. Both energy and mass are transferred from the system to surroundings and from the surroundings to system. (e.g). Air compressor (Fig.5),. I.C. Engines, 3. Turbines, 4. Boilers, 5. Centrifugal pumps, 6. Nozzles. Most of the engineering devices are open systems.. ISOLATED SYSTEM Neither energy nor mass transfer occurs between the system and surroundings (Fig.7). Practically, no system is isolated. Both mass and energy can cross the boundaries of a control volume. Surrounding System No mass transfer No energy trasfer Fig..7. HOMOGENEOUS AND HETEROGENEOUS SYSTEMS A system, which contains only a single phase, is called as Homogeneous system. Eg. Mixture of air and water vapour. A system, which consists of more than one phase, is called as Heterogeneous system. Eg. Mixture of water and steam.

. Thermodynamics - www.airwalkpublications.com.. Pure substance A Substance with homogeneous and invariable chemical composition even though change of phase takes place is called as pure substance. Eg. Water... State postulate The number of independent intensive properties are required to fix the state of the system is given by state postulate. For a pure substance, this is called as two property rule. i.e., two intensive properties are required to fix the state of the pure substance. Number of independent intensive properties can be found analytically using Gibb s rule P F C P - No. of phase, C - No. of components F - No. of independent intensive properties eg: For single liquid (or) single gas P, C F C P.3 PROPERTY It is a characteristic of the system. The system is identified by some quantities like temperature, pressure, volume etc.. Intensive Property: The properties which do not depend on the mass of the system, are called intensive property. Intensive property - Independent of the mass of the system: Example - Temperature, pressure, density, surface tension, specific gravity, etc.. Extensive Property: Those properties which depend on the mass of the system are called extensive property. Example: Volume, Force, eg: electric charge, weight, energy (heat and work) magnetization. If mass is more, then volume will be more. (Fig.8). Extensive properties Intensive properties Criteria to differentiate intensive and extensive properties. Fig..8

Basic Concepts and Zeroth Law of Thermodynamics.3 The extensive property divided by mass will become intensive property. (e.g) Volume m 3 / mass Specific volume m 3 /kg Extensive Intensive Enthalpy kj /mass Specific enthalpy kj/kg Extensive Intensive Generally, upper case letters are used to denote extensive properties (with mass m being a major exception), and lowercase letters are used for intensive properties (with pressure P and temperature T being the obvious exceptions)..4 STATE, PATH AND PROCESS Consider a system does not undergoing any change. At this point, all the properties can be measured (or) calculated throughout the entire system, which gives us a set of properties that completely describes the condition, or the state, of the system. At a given state, all the properties of a system have fixed values. If the value of even one property changes, the state will change to a different one. A system is shown at different states in the Fig..9. Thermodynamics deals with equilibrium state. The word equilibrium implies a state of balance. In an equilibrium state, there are no unbalanced potentials (or driving forces) within the system. There are many types of equilibrium, and a system is not in thermodynamic equilibrium unless the conditions of all the relevant types of equilibrium are satisfied. For example, a system is in thermal equilibrium if the temperature is same throughout the entire system, as shown in Fig..0. That is, the system involves no temperature differential, which is the driving force for heat flow. m = 3kg T = 0 o C V =.5 m 3 m = 3kg T = 0 o C V = 3.5 m 3 ( a ) State ( b ) State A system at two different states Fig..9 ( a ) Before ( b ) After A closed system reaching therm al equilibrium Fig..0

.4 Thermodynamics - www.airwalkpublications.com Any change that a system undergoes from one equilibrium state to another is called a process, and the series of states through which a system passes during a process is called the path of the process. To describe a process completely, one should specify the initial and final states of the process, as well as the path it follows and the interactions with the surroundings. Refer the Fig.. The state is a condition of the system at particular time. Each and every condition of the system is called state. At state (), the pressure is P and the volume is V. Similarly at state (), X X X the pressure is P the volume is V. In between and, there are so many states A, B, C,, G. So every time the system is under the change of states. If all the states are traced, it is the path of the change of states. If the path is completely specified, the change of state is called process. The example given is a compression process..5 CYCLE The series of processes whose end states are identical, then it is called cycle. Refer Fig.. P The process A The process B Cycle B The process A and the process B form a cycle. Because initial state is and final state is also. So it is a cycle (or) thermodynamic cycle. A A system is said to have undergone a cycle, if it returns to its initial state at the V end of the process. That is, for a cycle, the initial and final states are identical. P P G F E D C B A X - State A- State G- State - State - = Process X X X V V V State State Fig.. Fig..

Basic Concepts and Zeroth Law of Thermodynamics.5.6 THERMODYNAMIC EQUILIBRIUM When mechanical equilibrium, chemical equilibrium and thermal equilibrium are satisfied, then the system is said to be in thermodynamic equilibrium. When any property remains same with respect to time, it is called as equilibrium or steady state. Eg. Temperature and pressure at all points of a system are same means that the system exists in thermodynamic equilibrium.. Mechanical Equilibrium If the system s pressure remains same with respect to time, then the system is said to be in mechanical equilibrium.. Chemical Equilibrium If the system s chemical composition remains same with respect to time, then the system is said to be in chemical equilibrium. 3. Thermal Equilibrium If the system s temperature remains same with respect to time, then the system is said to be in thermal equilibrium..7 QUASI-STATIC (OR) QUASI EQUILIBRIUM PROCESS When a process proceeds in such a manner that the system remains infinitesimally close to an equilibrium state at all times, it is called a quasi-static, (or) quasi-equilibrium process. A quasi-equilibrium process can be viewed as a sufficiently slow process that allows the system to adjust itself internally so that properties in one part of the system do not change any faster than those at other parts. A quasi-static process is an idealized process and is not a true representation of an actual process. But many actual processes closely approximate it and they can be modeled as quasi-equilibrium with negligible error. Engineers are interested in quasi-equilibrium processes for two reasons as follows.. They are easy to analyze.. Work-producing devices (like engine) deliver maximum work when they operate on quasi-static processes. Therefore, quasi-static processes serve as standards to which actual processes can be compared.

.6 Thermodynamics - www.airwalkpublications.com Stops C ylinder P P(Pressure) Final state Weight Stops P I S T O N P V T Initial state System boundary Weights C ylinder System boundary P P (Pressure) V V V(Volume) Equilibrium states Quasi-static process V (Volume) Fig..3 Quasi-Static process (or) Quasi-Equilibrium process Consider a system of gas contained in a cylinder Fig.3(a). The system initially is in equilibrium state P, V and t. The weight on the piston is balanced by the pressure of the gas. If the weight is removed, there will be an unbalanced force between the system and surroundings, and under the gas pressure, the piston will move up till it hits the stops. The system comes to an equilibrium state - P, V and t. But the inter-mediate states are non-equilibrium states and we cannot define its properties. So these two states ( and ) are joined by dotted line. Now instead of single weight, we can place many number of small weights on the piston Fig.3(b). If we remove weights one by one very slowly from the piston, then the piston will move upward very slowly. The change of state of system from equilibrium state is infinitesimally small. So

p Basic Concepts and Zeroth Law of Thermodynamics.7 every state traced by the system is equilibrium state. The process, joined by all the equilibrium states passed by the system is called quasi-static process. [ Quasi means almost ]. Quasi-static process is a reversible process. A process which can be reversed in direction and the system retraces the same equilibrium states is known as reversible process. Infinite slowness is the characteristic feature of a quasi-static process..8 PATH FUNCTION AND POINT FUNCTION Refer the Fig.4. In this fig, there are many quasi-static paths such as A, B or C from state to state. Since area under each curve represents the work for each process, the amount of work involved in path A, B and C are not equal. P The work is not a function of the end states of the process but it depends on the C path the system follows from state to state. Hence, work is called a path A B function and d W is inexact (or) P imperfect differential. V V Thermodynamic properties like V Work- a path function pressure, volume and temperature are point functions, because, for a given state, Fig..4 there is a definite value for each property. The change of property of a system is independent of the path the system follows during the change of state and it depends only on the initial and final states of the system. Hence dv (or) dp is an exact (or) perfect differentials. For example, the integration of property is W = 0 kj A W = 8 kj B W = 6 kj C V V dv V V i.e., Change in volume depends only on the end states of the system irrespective of the path the system follows. But, workdone in a quasi-static process between two given state depends on the path followed. And the integration of work transfer is

.8 Thermodynamics - www.airwalkpublications.com Rather, dw W W dw W.9 ZEROTH LAW OF THERMODYNAMICS If the systems A and B are in thermal equilibrium separately and A and C are in thermal equilibrium separately, then B and C should be in thermal equilibrium. This law is the basis for temperature measurement. Therm al equilibrium Thermal equilibrium.9. Equality of temperature When two bodies at different temperatures are brought into contact, after some time, they attains a common temperature and are then said to exist in thermal equilibrium. The zeroth law was first formulated by R.H Fowler. This law explains the fundamental principles of thermodynamics, but was recognised after the formulation of first and second laws of thermodynamics. So it was named as zeroth law since it should have preceded the first and second laws of thermodynamics..0 MEASUREMENT OF TEMPERATURE The temperature of a body can be measured, by using a device known as thermometer. A common thermometer consists of a small amount of mercury in an evacuated glass tube. There are five different kinds of thermometer.. Constant volume gas thermometer. Constant pressure gas thermometer 3. Electrical resistance thermometer 4. Thermocouple 5. Mercury-in-glass thermometer B A Fig..5 C

Basic Concepts and Zeroth Law of Thermodynamics.9.0. Thermometry Thermometry is the science and practice of temperature measurement. Any measurable change in the thermometric probe (eg: extension of mercury in the tube of mercury-in-glass thermometer) can be used to mark temperature levels, that should later be calibrated as internationally agreed unit (like celsius, Fahrenheit, Kelvin, etc...) Thermometry is broadly divided into two subfields. (i) Contact thermometry (ii) Non-contact thermometry.0. Applications of thermometry Temperature is one of the most measured physical parameters in science and technology, but thermometry is not only applied to measuring temperature, but also an indirect measure of many material properties like thermal capacities, relative humidity (by means of wet bulb (or) dew point temperatures) and enthalpy changes (by thermal analysis).. THERMOMETRIC PROPERTY Thermometric property is any physical property that changes measurably with temperature. eg: Extension of mercury in mercury-in-glass thermometer.. Reference points A reference point is a basis (or) a standard, for evaluation. To calibrate the thermometer, first and foremost, we need to define a temperature scale. For defining the temperature scale, we have to choose reference points (reference temperature) also called as the fixed points. For Example: In celsius scale, the fixed points are defined using the properties of pure water. i.e., the lower fixed point or ice point, is the temperature of pure melting ice at normal atmospheric pressure. Also, the higher fixed point or steam point, is the temperature of pure boiling water at normal atmospheric pressure. Fixed point or reference points are classified into two categories. (i) Two reference points method (or) two fixed points method (method used before 954) (ii) One reference point method (or) one fixed points method (method used after 954)

.0 Thermodynamics - www.airwalkpublications.com (i) Two reference points method In this method, two fixed points are used, i.e., (a) Ice point (b) Steam point (a) Ice point: Ice point is the temperature at which ice and water are in equilibrium at a pressure of atm pressure. (b) Steam point: Steam point is the temperature at which water vapour condenses at a pressure of atm pressure. Let X be the thermometric property and x be the temperature of the system to be measured, then x ax where a is arbitrary constant. The thermometer is first placed in contact with system whose temperature X to be measured & then in contact with one of the fixed point (steam or ice), whose temperature is X, Thus X X X X X X X X...() Similarly, the thermometer at the temperature s is placed in contact with another fixed point of temperature X. It gives Subtract () from () X X X X X X...() X X X X X X X X X X The temperature interval, X X between these two fixed points was chosen to be 00 degrees. The use of two fixed points was found unsatisfactory and later disregarded. (ii) One reference point method In this method, only one reference point is used.i.e., the triple point of water.