Applied thermodynamics of fluids / edited by A.R.H. Goodwin, J.V. Sengers, C.J. Peters.
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Year of Publication: | 2010 |
Language: | English |
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Physical Description: | xxiii, 509 p. :; ill. |
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Table of Contents:
- Machine generated contents note: ch. 1 Introduction / J. Peters
- References
- ch. 2 Fundamental Considerations / Cor J. Peters
- 2.1. Introduction
- 2.2. Basic Thermodynamics
- 2.2.1. Homogeneous Functions
- 2.2.2. Thermodynamic Properties from Differentiation of Fundamental Equations
- 2.3. Deviation Functions
- 2.3.1. Residual Functions
- 2.3.2. Evaluation of Residual Functions
- 2.4. Mixing and Departure Functions
- 2.4.1. Departure Functions with Temperature, Molar Volume and Composition as the Independent Variables
- 2.4.2. Departure Functions with Temperature, Pressure and Composition as the Independent Variables
- 2.5. Mixing and Excess Functions
- 2.6. Partial Molar Properties
- 2.7. Fugacity and Fugacity Coefficients
- 2.8. Activity Coefficients
- 2.9. The Phase Rule
- 2.10. Equilibrium Conditions
- 2.10.1. Phase Equilibria
- 2.10.2. Chemical Equilibria
- 2.11. Stability and the Critical State
- 2.11.1. Densities and Fields
- 2.11.2. Stability.
- 2.11.3. Critical State
- References
- ch. 3 The Virial Equation of State / J. P. Martin Trusler
- 3.1. Introduction
- 3.1.1. Temperature Dependence of the Virial Coefficients
- 3.1.2. Composition Dependence of the Virial Coefficients
- 3.1.3. Convergence of the Virial Series
- 3.1.4. The Pressure Series
- 3.2. Theoretical Background
- 3.2.1. Virial Coefficients of Hard-Core-Square-Well Molecules
- 3.3. Thermodynamic Properties of Gases
- 3.3.1. Perfect-gas and Residual Properties
- 3.3.2. Helmholtz Energy and Gibbs Energy
- 3.3.3. Perfect-Gas Properties
- 3.3.4. Residual Properties
- 3.4. Estimation of Second and Third Virial Coefficients
- 3.4.1. Application of Intermolecular Potential-energy Functions
- 3.4.2. Corresponding-states Methods
- References
- ch. 4 Cubic and Generalized van der Waals Equations of State / Ioannis G. Economou
- 4.1. Introduction
- 4.2. Cubic Equation of State Formulation
- 4.2.1. The van der Waals Equation of State (1873)
- 4.2.2. The Redlich and Kwong Equation of State (1949).
- 4.2.3. The Soave, Redlich and Kwong Equation of State (1972)
- 4.2.4. The Peng and Robinson Equation of State (1976)
- 4.2.5. The Patel and Teja (PT) Equation of State (1982)
- 4.2.6. The α Parameter
- 4.2.7. Volume Translation
- 4.2.8. The Elliott, Suresh and Donohue (ESD) Equation of State (1990)
- 4.2.9. Higher-Order Equations of State Rooted to the Cubic Equations of State
- 4.2.10. Extension of Cubic Equations of State to Mixtures
- 4.3. Applications
- 4.3.1. Pure Components
- 4.3.2. Oil and Gas Industry
- Hydrocarbons and Petroleum Fractions
- 4.3.3. Chemical Industry
- Polar and Hydrogen Bonding Fluids
- 4.3.4. Polymers
- 4.3.5. Transport Properties
- 4.4. Conclusions
- References
- ch. 5 Mixing and Combining Rules / Stanley I. Sandler
- 5.1. Introduction
- 5.2. The Virial Equation of State
- 5.3. Cubic Equations of State
- 5.3.1. Mixing Rules
- 5.3.2. Combining Rules
- 5.3.3. Non-Quadratic Mixing and Combining Rules
- 5.3.4. Mixing Rules that Combine an Equation of State with an Activity-Coefficient Model.
- 5.4. Multi-Parameter Equations of State
- 5.4.1. Benedict, Webb, and Rubin Equation of State
- 5.4.2. Generalization with the Acentric Factor
- 5.4.3. Helmholtz-Function Equations of State
- 5.5. Mixing Rules for Hard Spheres and Association
- 5.5.1. Mixing and Combining Rules for SAFT
- 5.5.2. Cubic Plus Association Equation of State
- References
- ch. 6 The Corresponding-States Principle / James F. Ely
- 6.1. Introduction
- 6.2. Theoretical Considerations
- 6.3. Determination of Shape Factors
- 6.3.1. Other Reference Fluids
- 6.3.2. Exact Shape Factors
- 6.3.3. Shape Factors from Generalized Equations of State
- 6.4. Mixtures
- 6.4.1. van der Waals One-Fluid Theory
- 6.4.2. Mixture Corresponding-States Relations
- 6.5. Applications of Corresponding-States Theory
- 6.5.1. Extended Corresponding-States for Natural Gas Systems
- 6.5.2. Extended Lee-Kesler
- 6.5.3. Generalized Crossover Cubic Equation of State
- 6.6. Conclusions
- References
- ch. 7 Thermodynamics of Fluids at Meso and Nano Scales / Christopher E. Bertrand.
- 7.1. Introduction
- 7.2. Thermodynamic Approach to Meso-Heterogeneous Systems
- 7.2.1. Equilibrium Fluctuations
- 7.2.2. Local Helmholtz Energy
- 7.3. Applications of Meso-Thermodynamics
- 7.3.1. Van der Waals Theory of a Smooth Interface
- 7.3.2. Polymer Chain in a Dilute Solution
- 7.3.3. Building a Nanoparticle Through Self Assembly
- 7.3.4. Modulated Fluid Phases
- 7.4. Meso-Thermodynamics of Criticality
- 7.4.1. Critical Fluctuations
- 7.4.2. Scaling Relations
- 7.4.3. Near-Critical Interface
- 7.4.4. Divergence of Tolman's Length
- 7.5. Competition of Meso-Scales
- 7.5.1. Crossover to Tricriticality in Polymer Solutions
- 7.5.2. Tolman's Length in Polymer Solutions
- 7.5.3. Finite-size Scaling
- 7.6. Non-Equilibrium Meso-Thermodynamics of Fluid Phase Separation
- 7.6.1. Relaxation of Fluctuations
- 7.6.2. Critical Slowing Down
- 7.6.3. Homogeneous Nucleation
- 7.6.4. Spinodal Decomposition
- 7.7. Conclusion
- References
- ch. 8 SAFT Associating Fluids and Fluid Mixtures / Amparo Galindo.
- 8.1. Introduction
- 8.2. Statistical Mechanical Theories of Association and Wertheim's Theory
- 8.3. SAFT Equations of State
- 8.3.1. SAFT-HS and SAFT-HR
- 8.3.2. Soft-SAFT
- 8.3.3. SAFT-VR
- 8.3.4. PC-SAFT
- 8.3.5. Summary
- 8.4. Extensions of the SAFT Approach
- 8.4.1. Modelling the Critical Region
- 8.4.2. Polar Fluids
- 8.4.3. Ion-Containing Fluids
- 8.4.4. Modelling Inhomogeneous Fluids
- 8.4.5. Dense Phases: Liquid Crystals and Solids
- 8.5. Parameter Estimation: Towards more Predictive Approaches
- 8.5.1. Pure-component Parameter Estimation
- 8.5.2. Use of Quantum Mechanics in SAFT Equations of State
- 8.5.3. Unlike Binary Intermolecular Parameters
- 8.6. SAFT Group-Contribution Approaches
- 8.6.1. Homonuclear Group-Contribution Models in SAFT
- 8.6.2. Heteronuclear Group Contribution Models in SAFT
- 8.7. Concluding Remarks
- References
- ch. 9 Polydisperse Fluids / Dieter Browarzik
- 9.1. Introduction
- 9.2. Influence of Polydispersity on the Liquid + Liquid Equilibrium of a Polymer Solution.
- 9.3. Approaches to Polydispersity
- 9.3.1. The Pseudo-component Method
- 9.3.2. Continuous Thermodynamics
- 9.4. Application to Real Systems
- 9.4.1. Polymer Systems
- 9.4.2. Petroleum Fluids, Asphaltenes, Waxes and Other Applications
- 9.5. Conclusions
- References
- ch. 10 Thermodynamic Behaviour of Fluids near Critical Points / Mikhail A. Anisimov
- 10.1. Introduction
- 10.2. General Theory of Critical Behaviour
- 10.2.1. Scaling Fields, Critical Exponents, and Critical Amplitudes
- 10.2.2. Parametric Equation of State
- 10.3. One-Component Fluids
- 10.3.1. Simple Scaling
- 10.3.2. Revised Scaling
- 10.3.3. Complete Scaling
- 10.3.4. Vapour-Liquid Equilibrium
- 10.3.5. Symmetric Corrections to Scaling
- 10.4. Binary Fluid Mixtures
- 10.4.1. Isomorphic Critical Behaviour of Mixtures
- 10.4.2. Incompressible Liquid Mixtures
- 10.4.3. Weakly Compressible Liquid Mixtures
- 10.4.4. Compressible Fluid Mixtures
- 10.4.5. Dilute Solutions
- 10.5. Crossover Critical Behaviour
- 10.5.1. Crossover from Ising-like to Mean-Field Critical Behaviour.
- 10.5.2. Effective Critical Exponents
- 10.5.3. Global Crossover Behaviour of Fluids
- 10.6. Discussion
- Acknowledgements
- References
- ch. 11 Phase Behaviour of Ionic Liquid Systems / Cor J. Peters
- 11.1. Introduction
- 11.2. Phase Behaviour of Binary Ionic Liquid Systems
- 11.2.1. Phase Behaviour of (Ionic Liquid + Gas Mixtures)
- 11.2.2. Phase Behaviour of (Ionic Liquid + Water)
- 11.2.3. Phase Behaviour of (Ionic Liquid + Organic)
- 11.3. Phase Behaviour of Ternary Ionic Liquid Systems
- 11.3.1. Phase Behaviour of (Ionic Liquid + Carbon Dioxide + Organic)
- 11.3.2. Phase Behaviour of (Ionic Liquid + Aliphatic + Aromatic)
- 11.3.3. Phase Behaviour of (Ionic Liquid + Water + Alcohol)
- 11.3.4. Phase Behaviour of Ionic Liquid Systems with Azeotropic Organic Mixtures
- 11.4. Modeling of the Phase Behaviour of Ionic Liquid Systems
- 11.4.1. Molecular Simulations
- 11.4.2. Excess Gibbs-energy Methods
- 11.4.3. Equation of State Modeling
- 11.4.4. Quantum Chemical Methods
- References
- ch. 12 Multi-parameter Equations of State for Pure Fluids and Mixtures / Roland Span.
- 12.1. Introduction
- 12.2. The Development of a Thermodynamic Property Formulation
- 12.3. Fitting an Equation of State to Experimental Data
- 12.3.1. Recent Nonlinear Fitting Methods
- 12.4. Pressure-Explicit Equations of State
- 12.4.1. Cubic Equations
- 12.4.2. The Benedict-Webb-Rubin Equation of State
- 12.4.3. The Bender Equation of State
- 12.4.4. The Jacobsen-Stewart Equation of State
- 12.4.5. Thermodynamic Properties from Pressure-Explicit Equations of State
- 12.5. Fundamental Equations
- 12.5.1. The Equation of Keenan, Keyes, Hill, and Moore
- 12.5.2. The Equations of Haar, Gallagher, and Kell
- 12.5.3. The Equation of Schmidt and Wagner
- 12.5.4. Reference Equations of Wagner
- 12.5.5. Technical Equations of Span and of Lemmon
- 12.5.6. Recent Equations of State.
- Note continued--
- 13.6. Concluding Remarks
- References
- ch. 14 Applied Non-Equilibrium Thermodynamics / Dick Bedeaux
- 14.1. Introduction
- 14.1.1. A Systematic Thermodynamic Theory for Transport
- 14.1.2. On the Validity of the Assumption of Local Equilibrium
- 14.1.3. Concluding remarks
- 14.2. Fluxes and Forces from the Second Law of Thermodynamics
- 14.2.1. Continuous phases
- 14.2.2. Maxwell-Stefan Equations
- 14.2.3. Discontinuous Systems
- 14.2.4. Concluding Remarks
- 14.3. Chemical Reactions
- 14.3.1. Thermal Diffusion in a Reacting System
- 14.3.2. Mesoscopic Description Along the Reaction Coordinate
- 14.3.3. Heterogeneous Catalysis
- 14.3.4. Concluding Remarks
- 14.4. The Path of Energy-Efficient Operation
- 14.4.1. An Optimisation Procedure
- 14.4.2. Optimal Heat Exchange
- 14.4.3. The Highway Hypothesis for a Chemical Reactor
- 14.4.4. Energy-Efficient Production of Hydrogen Gas
- 14.4. Conclusions
- References.