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Modeling of Liquid Phases [Kietas viršelis]

(Ecole des Mines de Saint-Etienne, France)
  • Formatas: Hardback, 260 pages, aukštis x plotis x storis: 241x165x19 mm, weight: 1361 g
  • Išleidimo metai: 11-Aug-2015
  • Leidėjas: ISTE Ltd and John Wiley & Sons Inc
  • ISBN-10: 1848218656
  • ISBN-13: 9781848218659
Kitos knygos pagal šią temą:
  • Formatas: Hardback, 260 pages, aukštis x plotis x storis: 241x165x19 mm, weight: 1361 g
  • Išleidimo metai: 11-Aug-2015
  • Leidėjas: ISTE Ltd and John Wiley & Sons Inc
  • ISBN-10: 1848218656
  • ISBN-13: 9781848218659
Kitos knygos pagal šią temą:

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 small sizes. Macroscopic and microscopic models are in turn covered with a constant correlation between the two scales. Particular attention has been given to the rigor of mathematical developments.

This second volume in the set is devoted to the study of liquid phases.

Preface xi
Notations And Symbols xv
Chapter 1 Pure Liquids 1(36)
1.1 Macroscopic modeling of liquids
1(1)
1.2 Distribution of molecules in a liquid
2(7)
1.2.1 Molecular structure of a non- associated liquid
3(1)
1.2.2 The radial distribution function
4(2)
1.2.3 The curve representative of the radial distribution function
6(2)
1.2.4 Calculation of the macroscopic thermodynamic values
8(1)
1.3 Models extrapolated from gases or solids
9(7)
1.3.1 Guggenheim's smoothed potential model
10(3)
1.3.2 Mie's harmonic oscillator model
13(2)
1.3.3 Determination of the free volume on the basis of the dilation and the compressibility
15(1)
1.4 Lennard-Jones and Devonshire cellular model
16(9)
1.5 Cellular and vacancies model
25(4)
1.6 Eyring's semi-microscopic formulation of the vacancy model
29(3)
1.7 Comparison between the different microscopic models and experimental results
32(5)
Chapter 2 Macroscopic Modeling Of Liquid Molecular Solutions 37(24)
2.1 Macroscopic modeling of the Margules expansion
38(1)
2.2 General representation of a solution with several components
39(1)
2.3 Macroscopic modeling of the Wagner expansions
40(3)
2.3.1 Definition of the Wagner interaction coefficients
40(1)
2.3.2 Example of a ternary solution: experimental determination of Wagner's interaction coefficients
41(2)
2.4 Dilute ideal solutions
43(3)
2.4.1 Thermodynamic definition of a dilute ideal solution
43(1)
2.4.2 Activity coefficients of a component with a pure-substance reference
44(1)
2.4.3 Excess Gibbs energy of an ideal dilute solution
44(1)
2.4.4 Enthalpy of mixing for an ideal dilute solution
45(1)
2.4.5 Excess entropy of a dilute ideal solution
46(1)
2.4.6 Molar heat capacity of an ideal dilute solution at constant pressure
46(1)
2.5 Associated solutions
46(11)
2.5.1 Example of the study of an associated solution
47(2)
2.5.2 Relations between the chemical potentials of the associated solution
49(1)
2.5.3 Calculating the extent of the equilibrium in an associated solution
50(1)
2.5.4 Calculating the activity coefficients in an associated solution
50(1)
2.5.5 Definition of a regular solution
51(1)
2.5.6 Strictly-regular solutions
52(1)
2.5.7 Macroscopic modeling of strictly-regular binary solutions
53(3)
2.5.8 Extension of the model of a strictly-regular solution to solutions with more than two components
56(1)
2.6 Athermic solutions
57(4)
2.6.1 Thermodynamic definition of an athermic solution
58(1)
2.6.2 Variation of the activity coefficients with temperature in an athermic solution
58(1)
2.6.3 Molar entropy and Gibbs energy of mixing for an athermic solution
58(1)
2.6.4 Molar heat capacity of an athermic solution
59(2)
Chapter 3 Microscopic Modeling Of Liquid Molecular Solutions 61(56)
3.1 Models of binary solutions with molecules of similar dimensions
62(12)
3.1.1 The microscopic model of a perfect solution
68(2)
3.1.2 Microscopic description of strictly-regular solutions
70(2)
3.1.3 Microscopic modeling of an ideal dilute solution
72(2)
3.2 The concept of local composition
74(13)
3.2.1 The concept of local composition in a solution
74(2)
3.2.2 Energy balance of the mixture
76(2)
3.2.3 Warren and Cowley's order parameter
78(2)
3.2.4 Model of Fowler & Guggenheim's quasi-chemical solution
80(7)
3.3 The quasi-chemical method of modeling solutions
87(5)
3.4 Difference of the molar volumes: the combination term
92(9)
3.4.1 Combinatorial excess entropy
92(5)
3.4.2 Flory's athermic solution model
97(1)
3.4.3 Staverman's corrective factor
98(3)
3.5 Combination of the different concepts: the UNIQUAC model
101(6)
3.6 The concept of contribution of groups: the UNIFAC model
107(10)
3.6.1 The concept of the contribution of groups
108(1)
3.6.2 The UNIFAC model
108(6)
3.6.3 The modified UNIFAC model (Dortmund)
114(1)
3.6.4 Use of the UNIFAC system in the UNIQUAC model
114(3)
Chapter 4 Ionic Solutions 117(42)
4.1 Reference state, unit of composition and activity coefficients of ionic solutions
119(2)
4.2 Debye and Hiickel's electrostatic model
121(29)
4.2.1 Presentation of the problem
122(1)
4.2.2 Notations
123(1)
4.2.3 Poisson's equation
124(1)
4.2.4 Electrical potential due to the ionic atmosphere
125(2)
4.2.5 Debye and Mickel's hypotheses
127(5)
4.2.6 Debye and Hiickel's solution for the potential due to the ionic atmosphere
132(2)
4.2.7 Charge and radius of the ionic atmosphere of an ion
134(2)
4.2.8 Excess Helmholtz energy and excess Gibbs energy due to charges
136(2)
4.2.9 Activity coefficients of the ions and mean activity coefficient of the solution
138(3)
4.2.10 Self-consistency of Debye and Hilckel's model
141(3)
4.2.11 Switching from concentrations to molalities
144(2)
4.2.12 Debye and HtIckel's law: validity and comparison with experimental data
146(1)
4.2.13 Debye and Mickel's limit law
147(1)
4.2.14 Extensions of Debye and Mickel's law
148(2)
4.3 Pitzer's model
150(5)
4.4 UNIQUAC model extended to ionic solutions
155(4)
Chapter 5 Determination Of The Activity Of A Component Of A Solution 159(22)
5.1 Calculation of an activity coefficient when we know other coefficients
160(4)
5.1.1 Calculation of the activity of a component when we know that of the other components in the solution
160(2)
5.1.2 Determination of the activity of a component at one temperature if we know its activity at another temperature
162(2)
5.2 Determination of the activity on the basis of the measured vapor pressure
164(4)
5.2.1 Measurement by the direct method
165(1)
5.2.2 Method using the vaporization constant in reference 11
166(2)
5.3 Measurement of the activity of the solvent of the basis of the colligative properties
168(5)
5.3.1 Use of measuring of the depression of the boiling point - ebullioscopy
168(2)
5.3.2 Use of measuring of the depression of the freezing point - cryoscopy
170(2)
5.3.3 Use of the measurement of osmotic pressure
172(1)
5.4 Measuring the activity on the basis of solubility measurements
173(3)
5.4.1 Measuring the solubilities in molecular solutions
174(1)
5.4.2 Measuring the solubilities in ionic solutions
174(2)
5.5 Measuring the activity by measuring the distribution of a solute between two immiscible solvents
176(1)
5.6 Activity in a conductive solution
176(5)
5.6.1 Measuring the activity in a strong electrolyte
176(4)
5.6.2 Determination of the mean activity of a weak electrolyte on the basis of the dissociation equilibrium
180(1)
Appendices 181(40)
Appendix 1
183(10)
Appendix 2
193(14)
Appendix 3
207(14)
Bibliography 221(4)
Index 225
Michel SOUSTELLE is a chemical engineer and Emeritus Professor at Ecole des Mines de Saint-Etienne in France. He taught chemical kinetics from postgraduate to Master degree level while also carrying out research in this topic.