multicomponent systems doba jackson, ph.d. huntingdon college

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Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

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Page 1: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Multicomponent systemsDoba Jackson, Ph.D.

Huntingdon College

Page 2: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Problem 1: Acetone has a normal boiling point of 56.2*C and a molar enthalpy of vaporization of 31.97 kJ/mol. Calculate the equilibrium vapor pressure of acetone at 20.0*C.

Page 3: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Problem 2: The vapor pressure of bromine is 133 torr at 20.0*C and 48.1 torr at 0.00*C. Calculate the enthalpy of vaporization of bromine.

Page 4: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Chemical Potentials of Liquids and liquid mixturesP

= RTLnPA

A AA

**

P= RTLn

PA

A AA

Θ is pressure at 1 bar

* is pressure of pure A

Rauolt’s Law*

A A AP P*A

AA

P

P

*= RTLnA A A

Rauolt’s law states that the chemical potentialof the liquid is altered by the presence of a solute.The amount of the deviation is based on the molefraction of the solute.

Page 5: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Ideal Solutions

• Ideal solutions are solutions that obey Rauolt’s law throughout its composition range from pure A to pure B.

Page 6: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Rauolt’s Law is observed when two solutions have similar structures

Obey’s Rauolt’s Law Does not obey’s Rauolt’s Law

Page 7: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Dilute solutions typically do not obey Rauolt’s Law but follows Henry’s Law

P= RTLn

PA

A AA

**

P= RTLn

PA

A AA

Θ is pressure at 1 bar

* is pressure of pure A

Henry’s LawA A AP K AA

A

P

K

**

= RTLn A AA A

A

K

P

Henry’s law states that the chemical potentialof the liquid is altered by the presence of a solute.The amount of the deviation is based on the molefraction of the solute.

Page 8: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Vapor-Pressure Lowering of Solutions: Raoult’s Law

The vapor pressure of pure water at 25 °C is 23.76 mm Hg. What is the vapor pressure of a solution made from 1.00 mol glucose in 15.0 mol of water at 25 °C? Glucose is a nonvolatile solute.

Psoln = Psolv Xsolv

= 22.3 mm Hg1.00 mol + 15.0 mol

x23.76 mm Hg 15.0 mol=

Page 9: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Basis for Rauolt’s and Henry’s Law

*A A AP P

A A AP K

Rauolt’s Law

Henry’s Law

Page 10: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

General model of solutions

Page 11: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Problem 5.24a

• It is found that the normal boiling point of a binary solution of A and B with XA=.6589 is 88*C. At this temperature the vapor pressures of pure A and B are 129.6 kPa and 51.60 kPa, respectively.

• (a) Is the solution Ideal?• (b) What is the composition of the vapor

above the solution mixture?

Page 12: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Temperature-composition diagrams

• Distillation- separation of mixtures by withdrawing the more volatile component

in the vapor phase.

• Theoretical plates- number of vaporization-condensation steps required to achieve a given composition.

Page 13: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College
Page 14: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College
Page 15: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College
Page 16: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Theoretical Plates

# of Theoretical Plates depend on several factors:

- Temperature- Distillation Apparatus- Composition

- Vaporization temp. difference- Azeotropes

-Amount of each phase can be determined by the lever rule

Page 17: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Types of Phase Diagrams• Vapor Pressure-Composition Diagrams

– Upper Liquid Phase (P=1)– Bi-Phase intermediate (P=2)– Lower Vapor Phase (P=1)

• Liquid-Composition Diagrams– Upper vapor Phase– Bi-Phase intermediate– Lower vapor Phase

Two miscible liquids

Two partially miscible liquids

Azeotropic composition

Page 18: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Liquid-only Phase diagrams

Upper consolute temp. (Tuc)-

Is the temperature at whichboth liquids are miscible.

Inside the circle, two phasesexist.

Each composition is givenby the lever rule.

Hexane-Nitrobenzene

Page 19: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Liquid-only Phase diagrams

Lower consolute temp. (Tlc)-

Is the temperature at whichboth liquids are miscible.

Inside the circle, two phasesexist.

Each composition is givenby the lever rule.

Water-Triethanolamine

Page 20: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Liquid-only Phase diagrams

Lower consolute temp. (Tlc)-

Is the temperature at whichboth liquids are miscible.

Inside the circle, two phasesexist.

Each composition is givenby the lever rule.

Water-Nicotine solution

Page 21: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Liquid-only Phase diagrams

Page 22: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

A temperature-composition diagram in which boiling occurs before the

solution becomes miscible

Page 23: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Colligative Properties

• Colligative Properties- properties of solutions that depend only on the number of molecules present in a volume of solvent and not on the identity of the solute.

–Vapor Pressure lowering–Boiling Point Elevation–Freezing Point Depression–Osmosis

Page 24: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Osmosis

Osmosis: the spontaneous passage of a pure solvent intoa solution while separated by asemi-permeable membrane.

- Cell membrane transport - Dialysis - Blood Transfusions - Osmometry (M.W. determinations)

Osmotic Pressure (π): the pressure required to stop the influx of solvent.

Page 25: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Calculation of Osmotic Pressure

* P

A A mPG p p V dP

* P

A A mPp p V dP

Fundamental Equation;Assume const. Temperature

* = RTLnA A Ap p

Change in pressure is due to soluteconcentration in the solution.

RTLnP

m APV dP

RTLn 1m BV

Page 26: Multicomponent systems Doba Jackson, Ph.D. Huntingdon College

Calculation of Osmotic Pressure

RTLn 1m BV 1 B BLn

RTm BV B

BT

n

n

RT Bm

T

nV

n

T mn V VRT BV n

RT Bn

V

RT M Bn M

V

Molar Concentration

Assume the solute concentration is small