09.01 - Criteria for Phase Equilibrium
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- Chapter 1 - Basic concepts
- Chapter 2 - The energy balance
- Chapter 3 - Energy balances for composite systems.
- Chapter 4 - Entropy
- Chapter 5 - Thermodynamics of Processes
- Chapter 6 - Classical Thermodynamics - Generalization to any Fluid
- Chapter 7 - Engineering Equations of State for PVT Properties
- Chapter 8 - Departure functions
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Chapter 9 - Phase Equlibrium in a Pure Fluid
- 09.01 - Criteria for Phase Equilibrium
- 09.02 - The Clausius-Clapeyron Equation
- 09.03 - Shortcut Estimation of Saturation Properties
- 09.04 - Changes in Gibbs Energy with Pressure
- 09.05 - Fugacity and Fugacity Coefficient
- 09.06 - Fugacity Criteria for Phase Equilibria
- 09.07 - Calculation of Fugacity (Gases)
- 09.08 - Calculation of Fugacity (Liquids)
- 09.09 - Calculation of Fugacity (Solids)
- 09.10 - Saturation Conditions from an Equation of State
- 09.11 - Stable Roots and Saturation Conditions
- Chapter 10 - Introduction to Multicomponent Systems
- Chapter 11 - An Introduction to Activity Models
- Chapter 12 - Van der Waals Activity Models
- Chapter 13 - Local Composition Activity Models
- Chapter 14 - Liquid-liquid and solid-liquid equilibria
- Chapter 16 - Advanced Phase Diagrams
- Chapter 15 - Phase Equilibria in Mixtures by an Equation of State
- Chapter 17 - Reaction Equilibria
- Chapter 18 - Electrolyte Solutions
Phase Equilibrium Criterion - G(11min)
Phase equilibrium in a pure fluid (uakron, 11min) can be contemplated in terms of the following question: Suppose propane exists at a set temperature in an uninsulated piston/cylinder with half the volume as vapor and half as liquid. What is the final pressure when the piston is pressed down. A proper thermodynamic answer leads to the consideration of the Gibbs energy, with implications that open up an entire new world of problems to be solved related to equilibrium partitioning for pure fluids and mixtures.
Comprehension Questions:
1. Write dG for the total piston/cylinder system in terms of the individual phases.
2. What is the criterion for equilibrium in a pure fluid?
3. What is the stable state (L,V,L=V) when GL > GV ?
4. For the vdW fluid at 62C, 0.35 MPa, the following roots were obtained: ZL = 0.02598,
ZV = 0.92718, A=0.08608, B=0.01820. What is the stable state (L,V,L=V)?
5. For the vdW fluid at 62C, 0.25 MPa, the following roots were obtained: ZL = 0.01859,
ZV = 0.94910, A=0.061487, B=0.013000. What is the stable state (L,V,L=V)?
Hint: (G-Gig)/RT = -ln(Z-B)-A/Z + Z - 1 - ln(Z) where A=a*P/(R2T2); B=bP/RT; b=0.125*RTc/Pc