10.01 - Introduction to Phase Diagrams
Book navigation
- 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
- Chapter 9 - Phase Equlibrium in a Pure Fluid
-
Chapter 10 - Introduction to Multicomponent Systems
- 10.01 - Introduction to Phase Diagrams
- 10.02 - Vapor-Liquid Equilibrium (VLE) Calculations
- 10.03 - Binary VLE using Raoult's Law
- 10.04 - Multicomponent VLE & Raoult's Law Calculations
- 10.06 - Relating VLE to Distillation
- 10.07 - Nonideal Systems
- 10.08 - Concepts for Generalized Phase Equilibria
- 10.09 Mixture Properties for Ideal Gases
- 10.10 - Mixture Properties for Ideal Solutions
- 10.11 The Ideal Solution Approximation and Raoult's Law
- 10.12 Activity Coefficient and Fugacity Coefficient Approaches
- 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
Introduction to Phase Behavior
Introduction to Phase Behavior (9:37) (msu.edu)
Students tend to be distracted with the algorithms for bubble, dew, and flash, and often miss the important concepts of the relation of the calculations to the phase diagram. This screencast discusses the pure component endpoints, the trends in phase behavior at the bubble and dew conditions, and the qualitative relation between the P-x-y and T-x-y diagrams.
Comprehension Questions:
1. Referring to the Txy diagram on slide 3, estimate T, nature (ie. L,V, V+L, L+L), composition(s), and amount of the phase(s) for points: a, b. d, g.
2. Referring to the Txy diagram on slide 3, suppose we had T = 340K and zA = 0.40. Estimate T, nature (ie. L,V, V+L, L+L), composition(s), and amount of the phase(s) for that point.
3. Which component is more volatile, A or B?
Bubble, Dew, Flash Concepts and the Lever Rule (4:01) (msu.edu)
Bubble, Dew, Flash Concepts and the Lever Rule (4:01) (msu.edu)
Understanding what is present (known) and not present (unkown) for a given state of a system will help you decide which routine to use. Notation is introduced for liquids, vapor, and overall compositions. Also, the lever rule concept is used throughout the chemical engineering curriculum, but it is important to see how to use compositions for the lever rule.
Comprehension Questions:
1. Which variables are fixed and which do you need to find in each of the following:
a. Bubble temperature
b. Bubble pressure
c. Dew temperature
d. Dew pressure
e. Isothermal flash
f. Adiabatic flash