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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...

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Detalles Bibliográficos
Clasificación:Libro Electrónico
Autor principal: Soustelle, Michel (Autor)
Formato: Electrónico eBook
Idioma:Inglés
Publicado: London : Hoboken, New Jersey : ISTE ; Wiley, [2016]
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.