Phase transformations /
The book offers advanced students, in 7 volumes, successively characterization tools phases, the study of all types of phase, liquid, gas and solid, pure or multi-component, process engineering, chemical and electrochemical equilibria, the properties of surfaces and phases of small sizes. Macroscopi...
Clasificación: | Libro Electrónico |
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Autor principal: | |
Formato: | Electrónico eBook |
Idioma: | Inglés |
Publicado: |
London : Hoboken, New Jersey :
ISTE ; Wiley,
[2016]
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Colección: | Chemical engineering series: chemical thermodynamics set ;
volume 5 |
Temas: | |
Acceso en línea: | Texto completo |
Tabla de Contenidos:
- Cover
- Title Page
- Copyright
- Contents
- Preface
- Notations and Symbols
- 1: Phase Transformations of Pure Substances
- 1.1. Standard state: standard conditions of a transformation
- 1.2. Classification and general properties of phase transformations
- 1.2.1. First-order transformations and the Clapeyron relation
- 1.2.2. Second-order transformations
- 1.2.2.1. Ehrenfest equations
- 1.2.2.2. Landau theory
- 1.2.2.2.1. Symmetry and order parameters
- 1.2.2.2.2. Second-order transitions according to Landau
- 1.2.2.2.3. Critical exponents
- 1.2.2.2.4. Limitation of Landau's model
- 1.3. Liquid-vapor transformations and equilibrium states
- 1.3.1. Method of two equations of state, using the Clapeyron equation
- 1.3.2. Gibbs energy and fugacity method
- 1.3.3. Unique equation of state method
- 1.3.4. The region of the critical point and spinodal decomposition
- 1.3.5. Microscopic modeling
- 1.3.6. Liquid-vapor equilibrium in the presence of an inert gas
- 1.4. Solid-vapor transformations and equilibriums
- 1.4.1. Macroscopic treatment
- 1.4.2. Microscopic treatment
- 1.5. Transformations and solid-liquid equilibria
- 1.5.1. Macroscopic treatment
- 1.5.2. Microscopic treatment
- 1.6. Diagram for the pure substance and properties of the triple point
- 1.7. Allotropic and polymorphic varieties of a solid
- 1.7.1. Enantiotropy
- 1.7.2. Monotropy
- 1.7.3. Transition from enantiotropy to monotropy and vice versa
- 1.8. Mesomorphic states
- 2: Properties of Equilibria Between Binary Phases
- 2.1. Classification of equilibria between the phases of binary systems
- 2.2. General properties of two-phase binary systems
- 2.2.1. Equilibrium conditions for two-phase binary systems
- 2.2.2. Conditions of evolution of a two-phase binary system
- 2.3. Graphical representation of two-phase binary systems.
- 2.3.1. Gibbs energy graphs
- 2.3.2. Phase diagram in the mono- and bi-phase zones
- 2.3.2.1. Construction of the isobaric phase diagram in the mono- or biphasic regions
- 2.3.2.2. Properties of phase diagrams in regions with one or two phases
- 2.3.2.2.1. The lever rule or law of chemical moments
- 2.3.2.2.2. Crossing a line in the diagram
- 2.3.2.2.3. Gibbs-Konovalov theorem
- 2.3.2.2.4. The different types of azeotropic points
- 2.3.2.2.5. Property of the vertical axes at X1(Ü)=0 and X1(Ü)=1 in the phase diagram
- 2.3.2.3. Particular configurations of a diagram in the regions with one or two phases
- 2.3.2.3.1. One component is completely immiscible with the other
- 2.3.2.3.2. The two components may be entirely miscible with one another
- 2.3.3. Isobaric cooling curves
- 2.4. Isobaric representation of three-phase binary systems
- 2.4.1. Gibbs energy curve
- 2.4.2. Isobaric phase diagram in tri-phase regions
- 2.4.3. Isobaric cooling curves with tri-phase zones
- 2.5. Isothermal phase diagrams
- 2.6. Composition/composition curves
- 2.7. Activity of the components and consequences of Raoult's and Henry's laws
- 3: Equilibria Between Binary Condensed Phases
- 3.1. Equilibria between phases of the same nature: liquid-liquid or solid-solid
- 3.1.1. Thermodynamics of demixing
- 3.1.2. Demixing in the case of low reciprocal solubilities
- 3.1.3. Demixing of strictly-regular solutions
- 3.2. Liquid-solid systems
- 3.2.1. Thermodynamics of the equilibria between a liquid phase and a solid phase
- 3.2.2. Isobaric phase diagrams of equilibria between a solid and a liquid
- 3.2.2.1. Miscible components in all proportions in the two phases
- 3.2.2.2. Equilibria between a solid and a liquid with demixing of the solid phase
- 3.2.2.3. Equilibria between a solid and a liquid with demixing of the liquid phase.
- 3.2.2.4. Three-phase reactions in liquid-solid systems
- 3.2.2.5. Systems with formations of definite compounds
- 3.2.3. Solidus and liquidus in the vicinity of the pure substance
- 3.3. Equilibria between two solids with two polymorphic varieties of the solid
- 3.4. Applications of solid-liquid equilibria
- 3.4.1. Solubility of a solid in a liquid: Schröder-Le Châtelier law
- 3.4.1.1. Thermodynamics of solubility
- 3.4.1.2. Curves of solubility of salts in water
- 3.4.2. Determination of molar mass by cryometry
- 3.5. Membrane equilibria
- osmotic pressure
- 3.5.1. Thermodynamics of osmotic pressure
- 3.5.2. Osmotic pressure of infinitely-dilute solutions: the Van 't Hoff law
- 3.5.3. Application of osmotic pressure to the determination of the molar mass of polymers
- 3.5.4. Osmotic pressure of strictly-regular solutions
- 3.5.5. Osmotic pressure and the osmotic coefficient
- 4: Equilibria Between Binary Fluid Phases
- 4.1. Thermodynamics of liquid-vapor equilibrium in a binary system
- 4.2. Liquid-vapor equilibrium in perfect solutions far from the critical conditions
- 4.2.1. Partial pressures and total pressure of a perfect solution
- 4.2.2. Isothermal diagram of a perfect solution
- 4.2.3. Isobaric diagram of a perfect solution
- 4.2.4. Phase composition curve
- 4.3. Liquid-gas equilibria in ideal dilute solutions
- 4.4. Diagrams of the liquid-vapor equilibria in real solutions
- 4.4.1. Total miscibility in the liquid phase
- 4.4.1.1. Isobaric diagrams
- 4.4.1.2. Isothermal diagrams
- 4.4.1.3. Partial pressures and total pressure
- 4.4.2. Partial miscibility in the liquid phase, heteroazeotropes
- 4.5. Thermodynamics of liquid-vapor azeotropy
- 4.5.1. Relation between the pressure of the azeotrope and the activity coefficients of the liquid phase at the azeotropic composition.
- 4.5.2. Relation between the activity coefficient and the temperature of the azeotrope
- 4.6. Liquid-vapor equilibria and models of solutions
- 4.6.1. Liquid-vapor equilibria in strictly-regular solutions
- 4.6.1.1. Azeotropy of strictly-regular solutions
- 4.6.1.1.1. Relation between temperature and composition of the azeotrope
- 4.6.1.1.2. Relation between composition and pressure in the azeotrope
- 4.6.1.1.3. Relation between the pressure and temperature of the azeotrope
- 4.6.1.1.4. Condition for the existence of the azeotrope
- 4.6.1.2. Liquid-vapor equilibrium and demixing of the liquid
- 4.6.2. Liquid-vapor equilibrium in associated solutions
- 4.7. Liquid-vapor equilibria in the critical region
- 4.8. Applications of liquid-vapor equilibria
- 4.8.1. Solubility of a gas in a liquid
- 4.8.2. Determination of molar masses by tonometry
- 4.8.3. Determination of molar masses by ebulliometry
- 4.8.4. Continuous rectification or fractional distillation
- 4.8.4.1. Insufficiency of simple distillation
- 4.8.4.2. Rectification in the case of a single-spindle binary system
- 4.8.4.2.1. Feasibility of separation by fractional distillation
- 4.8.4.2.2. Total reflux operation
- theoretical trays
- 4.8.4.2.3. The Fenske equation
- 4.8.4.2.4. McCabe and Thiele diagram
- 4.8.4.2.5. Partial reflux operation. Sorel's equation
- 4.8.4.3. Fractional distillation in the presence of an azeotrope
- 5: Equilibria Between Ternary Fluid Phases
- 5.1. Representation of the composition of ternary systems
- 5.1.1. Symmetrical representation of the Gibbs triangle
- 5.1.2. Dissymmetrical representation of the right triangle
- 5.2. Representation of phase equilibria
- 5.2.1. Isothermal projections
- 5.2.2. Conjugate points and conodes
- 5.2.3. Isopleth sections
- 5.3. Equilibria in liquid phases with miscibility gaps.
- 5.3.1. Representation of the miscibility gap
- 5.3.2. Sharing in liquid-liquid systems
- 5.3.2.1. The shared substance has the same constitution in the two solvents
- 5.3.2.2. The shared substance does not have the same constitution in the two solvents
- 5.3.3. Application of sharing between two liquids to solvent extraction
- 5.3.3.1. Discontinuous extractions
- 5.3.3.2. Multi-stage counterflow extraction
- 5.4. Liquid-vapor systems
- 5.4.1. Isothermal and isopleth sections (boiling and dew)
- 5.4.2. Distillation trajectories
- 5.4.3. Systems with two distillation fields
- 5.4.4. Systems with three distillation fields
- 5.5. Examples of applications of ternary diagrams between fluid phases
- 5.5.1. Treatment of argentiferous lead
- 5.5.2. Purity of oil products: aniline point
- 5.5.3. Obtaining concentrated ethyl alcohol
- 6: Equilibria Between Condensed Ternary Fluid Phases
- 6.1. Solidification of a ternary system with total miscibility in the liquid state and in the solid state
- 6.2. Solidification of a ternary system with no miscibility and with a ternary eutectic
- 6.2.1. Invariant transformations of a liquid-solid ternary system
- 6.2.2. Representations of the ternary system with no miscibility in the solid state
- 6.2.2.1. The isobaric three-dimensional representation
- 6.2.2.2. Projection of an isothermal section
- 6.2.2.3. Cooling and solidification of a given liquid
- 6.2.2.4. Solidification trajectory
- 6.2.3. Lowering of the melting point of a binary system by the addition of a component
- 6.2.4. Slope at the ternary eutectic
- 6.3. Ternary systems with partial miscibilities in the solid state and ternary eutectic
- 6.4. Solidification of ternary systems with definite compounds
- 6.4.1. Ternary system with a binary definite compound binary with congruent melting.