Fundamentals of Technical Thermodynamics: Textbook for Engineering Students

This document was uploaded by one of our users. The uploader already confirmed that they had the permission to publish it. If you are author/publisher or own the copyright of this documents, please report to us by using this DMCA report form.

Simply click on the Download Book button.

Yes, Book downloads on Ebookily are 100% Free.

Sometimes the book is free on Amazon As well, so go ahead and hit "Search on Amazon"

This textbook presents the essential scientific principles of thermodynamics in a detailed and well-structured manner for practice-oriented teaching. It conveys analytically reliable knowledge with a view to engineering application and provides the key to a quick understanding of e.g. thermal machines, heat transfer, humid air and combustion. The present English edition - in comparison to earlier German editions - has been extended to include aspects of fluid mechanics, dynamics of ideal gases and chemical thermodynamics.

Author(s): Martin Dehli, Ernst Doering, Herbert Schedwill
Publisher: Springer
Year: 2022

Language: English
Pages: 621
City: Wiesbaden

Foreword
Table of Contents
Important Formula Characters
Authors Vita
1 Basic Thermodynamic Terms
1.1 Applications of Thermodynamics
1.2 System
1.3 State, State Variables, Changes of State
1.4 Process, Process Variables
2 The First Law of Thermodynamics
2.1 The Principle of Conservation of Energy
2.2 Potential Energy
2.3 Kinetic Energy
2.4 Work
2.4.1 Volume Change Work
2.4.2 Coupling Work
2.4.3 Shift Work
2.4.4 Pressure Change Work
2.4.5 Friction Work
2.5 Thermal Energy
2.5.1 Internal Energy
2.5.2 Heat
2.5.3 Enthalpy
2.6 Energy Balances
2.6.1 Energy Balance for the Closed System
2.6.2 Energy Balance for the Open System
2.7 Heat Capacity
2.7.1 Specific Heat Capacity
2.7.2 The Specific Heat Capacity of Gases
2.8 Fluid Mechanics
2.8.1 General Aspects
2.8.2 Flow Shapes
2.8.3 Friction and Roughness
2.8.4 Individual Resistances
2.8.5 Equivalent Pipe Length
3 The Second Law of Thermodynamics
3.1 The Statement of the Second Law
3.1.1 Reversible and Irreversible Processes
3.1.2 Quasi-Static Changes of State
3.2 Irreversible Processes
3.2.1 Friction
3.2.2 Temperature Equalisation
3.2.3 Pressure Equalisation
3.3 Entropy
3.3.1 Reversible Substitute Processes of Adiabatic Processes
3.3.2 The Calculation of the Entropy Change
3.3.3 Entropy as a State Variable, Total Differential
3.4 The Entropy Change of Irreversible Processes
3.4.1 Friction
3.4.2 Temperature Equalisation
3.4.3 Pressure Equalisation
3.4.4 Throttling
3.5 Non-Adiabatic Process and Reversible Substitute Process
3.5.1 Isentropic Change of State; Interpretations of Entropy
3.5.2 Entropy Diagrams
3.5.3 Circular Integral, Thermodynamic Temperature
3.5.4 Dissipative Energy
4 Ideal
Gases
4.1 Thermal Equation of State
4.1.1 Law of Boyle and Mariotte
4.1.2 Law of Gay-Lussac
4.1.3 Physical Norm State
4.1.4 Gas Thermometer
4.1.5 Specific Gas Constant
4.1.6 Universal Gas Constant
4.2 Caloric State Variables of Ideal Gases
4.2.1 Internal Energy
4.2.2 Enthalpy
4.2.3 Entropy
4.3 Changes of State
4.3.1 Isochoric Change of State
4.3.2 Isobaric Change of State
4.3.3 Isothermal Change of State
4.3.4 Isentropic Change of State
4.3.5 Polytropic Change of State
4.3.6 Changes of State with Variable Mass
4.4 Specific Thermal Energy and Specific
Work in the T,s Diagram
4.5 Mixtures of Ideal Gases
4.5.1 The Mixing Process in the Closed System
4.5.2 The Mixing Process Without Total Volume Change
4.5.3 The Mixing Process
Without Temperature Change, Pressure Change and Total Volume Change
4.5.4 The Mixing Process in the Open System
4.6 Dynamics of Ideal Gases: Compressible Stationary Gas Flow
4.6.1 Introduction
4.6.2 Velocity of Sound and Propagation of Sound
4.6.3 Energy Equation and Bernoulli Equation of Compressible
One-Dimensional Ideal Gas Flow
4.6.4 Stagnation State Variables and Critical State
4.6.5 The Velocity Diagram of the Specific Energy Equation
4.6.6 Flow Function
4.6.7 Isentropic Gas Flow in Nozzles and Orifices
4.6.8 Accelerated Compressible Flow
4.6.9 Compression Shock
5 Real Gases and Vapors
5.1 Properties of Vapors
5.1.1 Phase Transitions
5.1.2 Two-Phase Regions
5.1.3 Boiling and Condensing
5.1.4 Evaporation and Thawing
5.1.5 Liquid
5.1.6 Two-Phase Liquid-Vapor State
5.1.7 Superheated Vapor
5.2 State Diagrams
5.2.1 The p,v,T Surface
5.2.2 The T,s Diagram
5.2.3 The h,s Diagram
5.3 Thermal Equations of State
5.3.1 The van der Waals Equation
5.3.2 The Boundary Curve and the Maxwell Relation
5.3.3 The Reduced van der Waals Equation
5.3.4 Different Approaches
5.3.5 Virial Coefficients
5.4 Calculation of State Variables; Property Tables
5.4.1 The Caloric State Variables
5.4.2 The Specific Heat Capacities cp and cv
5.4.3 The Isentropic Exponent and the Isothermal Exponent
5.4.4 The Clausius-Clapeyron Equation
5.4.5 Free Energy and Free Enthalpy
5.4.5.1 General
5.4.5.2 A g,s Diagram for Water and Steam
5.4.6 The Joule-Thomson Effect
6 Thermal
Machines
6.1 Classification and Types of Machines
6.1.1 Classification According to the Direction of Energy Conversion
6.1.2 Classification According to the Construction of the Machines
6.1.3 Classification According to the Type of Process Taking Place
6.2 Ideal Machines
6.2.1 Compression and Expansion in Ideal Machines
6.2.2 Multi-Stage Compression and Expansion
6.2.3 The Energy Balance for Flow Machines
6.2.4 The Energy Balance for Displacement Machines
6.3 Energy Balances for Real Machines
6.3.1 Internal or Indexed Work
6.3.2 Total Work
6.3.3 Total Enthalpy
6.4 Real Machines
6.4.1 The Uncooled Compressor
6.4.2 The Cooled Compressor
6.4.3 Piston Compressor
6.4.4 Turbo Compressor
6.4.5 Gas and Steam Turbines
6.5 Efficiencies
6.5.1 Comparison Processes
6.5.2 The Internal Efficiency
6.5.3 The Mechanical Efficiency
6.5.4 The Total Efficiency
6.5.5 The Isentropic Efficiency
6.5.6 The Isothermal Efficiency
6.5.7 The Polytropic Efficiency
7 Cyclic Processes
7.1 Cyclic Process Work, Heat Input and Heat Output
7.2 Right-Hand and Left-Hand Cyclic Processes
7.3 The Theory of Right-Hand Cyclic Processes
7.3.1 Conversion of Thermal to Mechanical Energy
7.3.2 Thermal Efficiency
7.3.3 Right-Hand Carnot Process
7.3.4 Effect of Irreversible Processes
7.3.5 Carnot Factor
7.4 Technically Used Right-Hand Cyclic Processes
7.4.1 Seiliger Process, Otto Process, Diesel Process,
Generalised Diesel Process
7.4.2 Joule Process
7.4.3 Ericsson Process
7.4.4 Stirling Process
7.4.5 Single-Polytropic Carnot Process
7.4.6 Gas Expansion Process
7.4.7 Clausius-Rankine Process
7.5 Comparative Evaluation
of Right-Hand Cyclic Processes
7.5.1 Process Variables and Cyclic Processes
7.5.2 Mechanical Effort Ratios and Thermal Effort Ratios
7.5.3 Evaluation Criteria For Important Thermodynamic Cyclic Processes
7.5.3.1 General Thermodynamic Relations
7.5.3.2 Examples
7.5.3.3 Graphical Representation of the Thermodynamic Relations
7.5.3.4 Cyclic Process Calculations for Real Fluids
7.6 Left-Hand Cyclic Processes
7.6.1 Performance Number
7.6.2 Left-Hand Carnot Process
7.6.3 Left-Hand Joule Process
7.6.4 Gas Expansion Process as a Left-Hand Cycle Process
7.6.5 Cold Vapor Compression Process
8 Exergy
8.1 Energy and Exergy
8.1.1 Exergy of Heat
8.1.2 Exergy of Bound Energy
8.1.3 Exergy of Temperature Change Heat
8.1.4 Exergy of Volume Change Work
8.1.5 Exergy of Shift Work
8.1.6 Exergy of Pressure Change Work
8.1.7 Exergy of Internal Energy
8.1.8 Exergy of Enthalpy
8.1.9 Exergy of Free Energy
8.1.10 Exergy of Free Enthalpy
8.1.11 Difference between EU and EF
8.1.12 Difference between EH and EG
8.1.13 Free Energy and Free Enthalpy as Thermodynamic Potentials
8.2 Exergy and Anergy
8.2.1 Anergy in a p, V Diagram and in a T,S Diagram
8.2.2 Anergy-Free Energies
8.3 Exergy Loss
8.3.1 Irreversibility and Exergy Loss
8.3.2 Exergy Loss and Anergy Gain
8.3.3 Exergetic Efficiencies
9 Heat
Transfer
9.1 Heat Radiation
9.1.1 Stefan-Boltzmann Law
9.1.2 Kirchhoff ’s Law
9.1.3 Planck’s Radiation Law
9.1.4 Wien’s Displacement Law
9.1.5 Lambert’s Cosine Law
9.1.6 Irradiance Number
9.2 Radiation Exchange
9.2.1 Cavity Method
9.2.2 Envelopment of One Surface by Another
9.2.3 Two Parallel Surfaces of Equal Size
9.2.4 Matrix Representation
9.3 Stationary One-Dimensional Heat Conduction
9.3.1 Plane Wall
9.3.2 Pipe Wall
9.4 Instationary One-Dimensional Heat Conduction
9.4.1 Plane Single-Layer Wall
9.4.2 Semi-Infinite Body
9.5 Heat Transfer by Convection
9.5.1 Heat Transfer Coefficient
9.5.2 Similarity Theory
9.5.3 Reynolds Analogy
9.5.4 Prandtl Analogy
9.5.5 Power Number Approaches for Laminar and Turbulent Flow
9.5.6 Approaches for Phase Transitions
9.6 Over-All Heat Transfer
9.6.1 Over-All Heat Transfer Coefficient
9.6.2 Fin Efficiency and Area Efficiency
9.6.3 Mean Temperature Difference
9.6.4 Operating Characteristic (Effectiveness)
9.7 Finned Heat Transfer Surfaces
9.7.1 Straight Fin with Rectangular Cross-Section
9.7.2 Circular Fin with Rectangular Cross-Section
9.8 Partition Wall Heat Exchangers
9.8.1 Unidirectional Flow Heat Exchanger
9.8.2 Counterflow Heat Exchanger
9.8.3 Crossflow Heat Exchanger
9.8.4 Heat Transfer with Phase Transition in a Heat Exchanger
9.9 Evaluation and Design
9.9.1 Correction Factor for a Crossflow Heat Exchanger
9.9.2 Representation of the Operating Characteristic
9.9.3 Longitudinal Heat Conduction in a Plane Partition Wall
9.9.4 Design Diagram
10 Humid Air
10.1 State Variables of Humid Air
10.1.1 Relative Humidity
10.1.2 Humidity Ratio and Saturation
10.1.3 Specific Enthalpy
10.2 Changes of State of Humid Air
10.2.1 Temperature Change
10.2.2 Humidification and Dehumidification
10.2.3 Mixing of Two Humid Air Quantities
10.3 The h,x Diagram of Mollier
10.3.1 Temperature Change
10.3.2 Humidification and Dehumidification
10.3.3 Mixing of Two Humid Air Quantities
10.4 Evaporation Model
10.4.1 Evaporation Coefficient
10.4.2 Energy Balances
10.4.3 Lewis Relationship
10.5 Cooling Limit
10.6 Evaporation and Dew Precipitation
10.7 Water Vapor Diffusion Through Walls
11 Combustion
11.1 Fuels
11.1.1 Gaseous Fuels
11.1.2 Solid and Liquid Fuels
11.1.3 Composition of the Combustion Gas,
Combustion Triangles, Combustion Control
11.2 Technical Aspects of Combustion
11.2.1 Initiation and Progression of Combustion
11.2.2 Complete and Incomplete Combustion
11.2.3 Dew Point of Combustion Gases
11.2.4 Chimney Draught
11.3 Upper Calorific Value and Lower Calorific Value
11.4 Theoretical Combustion Temperature
12 Chemical Thermodynamics
12.1 Systems Involving Chemical Reactions
12.2 Reaction Turnover and Reaction Rate
12.3 Molar Enthalpies of Reaction and Standard Molar Enthalpies
of Formation; Theorem of Hess
12.3.1 Molar Enthalpies of Reaction
12.3.2 Standard Molar Enthalpies of Formation; Theorem of Hess
12.4 Absolute Molar Entropies; Third Law of Thermodynamics
12.5 The Importance of the Second Law
for Chemical Reactions
12.6 Chemical Exergies
12.7 Fuel Exergies
12.8 Chemical Potentials
12.9 The Law of Mass Action
12.10 Pressure and Temperature Dependence of the Constants
of the Law of Mass Action; Law of Le Chatelier and Braun
12.11 Model of Isothermal-Isobaric Reversible Chemical Reactions
12.11.1 Model of Reversible Oxidation of Hydrogen
12.11.2 Model of Arbitrary Homogeneous Reversible Chemical Reactions
of Ideal Gases
12.11.3 Reversible Storage of Heat and Work in the Form of Chemical
Energy
12.12 Fuel Cells
Appendix
References
Index