Modeling of liquid phases /
This book is part of a set of books which offers advanced students successive characterization tool phases, the study of all types of phase (liquid, gas and solid, pure or multi-component), process engineering, chemical and electrochemical equilibria, and the properties of surfaces and phases of sma...
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| Format: | eBook |
| Language: | English |
| Published: |
London : Hoboken, NJ :
ISTE ; Wiley,
2015.
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| Series: | Chemical engineering series (ISTE Ltd). Chemical thermodynamics set ;
volume 2. |
| Subjects: | |
| Online Access: | Connect to the full text of this electronic book |
Table of Contents:
- Cover
- Title Page
- Copyright
- Contents
- Preface
- Notations and Symbols
- 1: Pure Liquids
- 1.1. Macroscopic modeling of liquids
- 1.2. Distribution of molecules in a liquid
- 1.2.1. Molecular structure of a non-associated liquid
- 1.2.2. The radial distribution function
- 1.2.3 The curve representative of the radial distribution function
- 1.2.4. Calculation of the macroscopic thermodynamic values
- 1.3. Models extrapolated from gases or solids
- 1.3.1. Guggenheim's smoothed potential model
- 1.3.2. Mie's harmonic oscillator model
- 1.3.3. Determination of the free volume on the basis of the dilation and the compressibility
- 1.4. Lennard-Jones and Devonshire cellular model
- 1.5. Cellular and vacancies model
- 1.6. Eyring's semi-microscopic formulation of the vacancy model
- 1.7. Comparison between the different microscopic models and experimental results
- 2: Macroscopic Modeling of Liquid Molecular Solutions
- 2.1. Macroscopic modeling of the Margules expansion
- 2.2. General representation of a solution with several components
- 2.3. Macroscopic modeling of the Wagner expansions
- 2.3.1. Definition of the Wagner interaction coefficients
- 2.3.2. Example of a ternary solution: experimental determination of Wagner's interaction coefficients
- 2.4. Dilute ideal solutions
- 2.4.1. Thermodynamic definition of a dilute ideal solution
- 2.4.2. Activity coefficients of a component with a pure-substance reference
- 2.4.3. Excess Gibbs energy of an ideal dilute solution
- 2.4.4. Enthalpy of mixing for an ideal dilute solution
- 2.4.5. Excess entropy of a dilute ideal solution
- 2.4.6. Molar heat capacity of an ideal dilute solution at constant pressure
- 2.5. Associated solutions
- 2.5.1. Example of the study of an associated solution
- 2.5.2. Relations between the chemical potentials of the associated solution.
- 2.5.3. Calculating the extent of the equilibrium in an associated solution
- 2.5.4. Calculating the activity coefficients in an associated solution
- 2.5.5. Definition of a regular solution
- 2.5.6. Strictly-regular solutions
- 2.5.7. Macroscopic modeling of strictly-regular binary solutions
- 2.5.8. Extension of the model of a strictly-regular solution to solutions with more than two components
- 2.6. Athermic solutions
- 2.6.1. Thermodynamic definition of an athermic solution
- 2.6.2. Variation of the activity coefficients with temperature in an athermic solution
- 2.6.3. Molar entropy and Gibbs energy of mixing for an athermic solution
- 2.6.4. Molar heat capacity of an athermic solution
- 3: Microscopic Modeling of Liquid Molecular Solutions
- 3.1. Models of binary solutions with molecules of similar dimensions
- 3.1.1. The microscopic model of a perfect solution
- 3.1.2. Microscopic description of strictly-regular solutions
- 3.1.3. Microscopic modeling of an ideal dilute solution
- 3.2. The concept of local composition
- 3.2.1. The concept of local composition in a solution
- 3.2.2. Energy balance of the mixture
- 3.2.3. Warren and Cowley's order parameter
- 3.2.4. Model of Fowler & Guggenheim's quasi-chemical solution
- 3.3. The quasi-chemical method of modeling solutions
- 3.4. Difference of the molar volumes: the combination term
- 3.4.1. Combinatorial excess entropy
- 3.4.2. Flory's athermic solution model
- 3.4.3. Staverman's corrective factor
- 3.4.3.1. The concept of structural parameters
- 3.4.3.2. Staverman's model
- 3.5. Combination of the different concepts: the UNIQUAC model
- 3.6. The concept of contribution of groups: the UNIFAC model
- 3.6.1. The concept of the contribution of groups
- 3.6.2. The UNIFAC model
- 3.6.3. The modified UNIFAC model (Dortmund).
- 5.2.1. Measurement by the direct method
- 5.2.2. Method using the vaporization constant in reference II
- 5.3. Measurement of the activity of the solvent of the basis of the colligative properties
- 5.3.1. Use of measuring of the depression of the boiling point
- ebullioscopy
- 5.3.2. Use of measuring of the depression of the freezing point
- cryoscopy
- 5.3.3. Use of the measurement of osmotic pressure
- 5.4. Measuring the activity on the basis of solubility measurements
- 5.4.1. Measuring the solubilities in molecular solutions
- 5.4.2. Measuring the solubilities in ionic solutions
- 5.5. Measuring the activity by measuring the distribution of a solute between two immiscible solvents
- 5.6. Activity in a conductive solution
- 5.6.1. Measuring the activity in a strong electrolyte
- 5.6.1.1. Measuring the absolute activity of an ion
- 5.6.1.2. Measurement of the mean activity coefficient of a strong electrolyte
- 5.6.2. Determination of the mean activity of a weak electrolyte on the basis of the dissociation equilibrium
- Appendices
- Appendix 1: Statistical Methods of Numerical Simulation
- A.1.1. The physical bases of simulation
- A.1.2. Construction of the sample
- A.1.2.1. Truncation of the potential function
- A.1.2.2. Limitation of edge effects
- A.1.2.2.1. Periodic boundary condition
- A.1.2.2.2. Minimum-image convention
- A.1.2.3. Estimation of the duration of the calculation
- A.1.3. The main calculation methods
- A.1.3.1. The Monte-Carlo method
- A.1.3.2. The molecular dynamics method
- Appendix 2: Reminders of the Properties of Solutions
- A.2.1. Values attached to solutions
- A.2.2. Peculiar values and mixing values
- A.2.2.1. Definitions
- A.2.3. Characterization of the imperfection of a real solution
- A.2.4. Activity coefficients
- A.2.5. Activity coefficients and reference states.