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Objectives of this course are: (1)Learn about what Chemical Engineers do (2) Learn about basic chemical process units (3) Learn to analyze and solve material balance and energy balance problems. This handout includes: Phase Equilibrium, Graphical Methods for Phase Equilibrium, Vle Phase Diagrams, Boiling Point of N-Heptane, Lever Rule, Eutectic, Solid-Liquid Phase Diagrams, Butanol-Water Demo, Liquid-Liquid Equilibrium, Liquid-Liquid Ternary
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Generated from Raoult’s law using the DIPPR vapor pressure correlations
Mole Fraction n-pentane yi for vapor xi for liquid
n-pentane and n-heptane at 2 atm
Vapor
Liquid
Dew line
Bubble line
Mole Fraction n-pentane yi for vapor xi for liquid
n-pentane and n-heptane at 1.5 atm
Vapor
Liquid
Dew line
Bubble line
VLE Phase Diagrams
(4) 92% pentane
(5) 39% pentane
(6) 10.2 atm
Lever Rule
2 distinct phases and 2 components
n (^) F zA
nL x (^) A
nV yA
n (^) F zA
nL x (^) A
nV yA
y x
y z
x y
z y
n
n
n F zA
nL x (^) A
nV yA
n F zA
nL x (^) A
nV yA
A A
A A A A
A A F
L
LF V
Distance B
Distance A
xA zA yA
LF V
Distance B
Distance A
xA zA yA
Solid B + Eutectic Solid A + Eutectic
Solid B + Eutectic Solid A + Eutectic
Solid B + Eutectic Solid A + Eutectic
What phases are present for a mixture of 30% A at 320 K?
What phases are present for a mixture of 60% A at 320 K?
What phases are present for mixture of 50% A at 300 K?
For a mixture of 80% A, what phases are present at equilibrium at 310 K? How much of each phase is present?
Pure Solid B and solution with 52% A
Solution with 60% A
Solid B and solid eutectic of 65% A
Solid A and solution with 68% A 2/3.2 = 62.5% of material is solution, 37.5% solid A