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Thermodynamics and Kinetics
Lecture 14
Properties of Mixtures
Raoult’s Law
Henry’s Law
Activity
NC State University
Measures of concentration There are three measures of concentration:
molar concentration per unit volume (molarity)
c = n/(liter of solution)
molar concentration per unit mass (molality)
m = n/(kg of solution)
mole fraction
x j =n j
n ii
Ideal solutions Raoult's law states
Pj = xjPj*
where Pj* is the vapor pressure of pure component j.
The vapor pressure of component j in an ideal solution
is given by the product of its mole fraction and P j*.
The chemical potential can be expressed as:
mj = mj* + RTln(Pj/Pj
*)
where Pj* is vapor the pressure of the pure component j in
the standard state.
Ideal solutions The significance of this expression is that we can now
consider the equilibrium between vapor and solution to write:
mjsoln = mj
vap = mj0 + RTln(Pj/Pj
0)
but for the vapor Pj0 = 1 bar. In the limit that the vapor
becomes the pure vapor we have:
mj* = mj
vap* = mj0 + RTln(P*j/Pj
0)
Thus
mjsoln = mj
* + RTln(Pj/Pj*)
keeping in mind the notation * means the pure component.
Ideal solutions The equation below is central equation of binary solution
mixtures.
mjsoln = mj
* + RTln(Pj/Pj*)
Using Raoult's law xj = Pj/Pj* we see that the chemical
potential can be expressed as:
mjsoln = mj
* + RTln(xj)
This equation defines an ideal solution.
The free energy of mixing The free energy for formation of a solution from individual
components is given by
Since
Gsoln = n1m1 + n2m2 , G1* = n1m1* and G2* = n2m2*.
we have that
for an ideal solution there is no enthalpy of mixing. The
volume of the mixture also does not change for an ideal
solution. The entropy change can be obtained from
in agreement with a previous derivation.
Gmix = Gsoln
– G1
*– G2
*
Gmix = n1m1 + n2m2 – n1m1* – n2m2
*
= nRT x1ln x1 + x2ln x2
Two component phase diagrams The total vapor pressure over an ideal solution is given by
Ptotal = P1 + P2 = x1P1* + x2P2
* = (1 - x2)P1* + x2P2
*
= P1* + x2(P2
* - P1*)
A plot of the total pressure has the form of a straight line.
Liquid composition: specific example
Consider the example in the book of 1-propanol and
2-propanol, which have P1* = 20.9 torr and P2
* = 45.2 torr,
respectively. So in this example, the phase diagram has the
appearance:
The vapor mole fraction The value of the mole fraction in the vapor is not necessarily
equal to that of the liquid. In the vapor phase the relative
numbers of moles is given by Dalton's law. Applying Dalton's
law we find:
y1 = P1/Ptotal = x1P1*/Ptotal
or
y2 = P2/Ptotal = x2P2*/Ptotal
The vapor curve is not the same as the liquid line.
Deriving the vapor curve Using the equation of the liquid line we find:
When substituted into y2 = x2P2*/Ptotal we have
Solving for Ptotal we find:
x2 =Ptotal – P1
*
P2
*– P1
*
y2 =P2
*
Ptotal
Ptotal – P1
*
P2
*– P1
*
y2Ptotal = P2
* Ptotal – P1
*
P2
*– P1
*=
P2
*Ptotal
P2
*– P1
*–
P2
*P1
*
P2
*– P1
*
P2
*– y2 P2
*– P1
*Ptotal = P2
*P1
*
Ptotal =P2
*P1
*
P2
*– y2 P2
*– P1
*
The vapor curve The is shown in the Figure below. The purple line was
calculated using the Dalton's law expression. What lies
between the blue and purple lines? This is the two phase
region.
Two
Phase
Region
The two phase region If we pick a composition and pressure that is inside this
region then we can use a tie line to indicate the composition
of each phase.
Boiling in a two component system If we reduce the pressure above a two component mixture
of 1-propanol and 2-propanol with a mole fraction of 0.6
1-propanol what is the composition of the vapor?
What is the composition of the vapor? a. y2 = 0.60
b. y2 = 0.48
c. y2 = 0.78
d. y2 = 0.98
What is the composition of the vapor? a. y2 = 0.60
b. y2 = 0.48
c. y2 = 0.78
d. y2 = 0.98
Boiling in a two component system If we continue to reduce the pressure the system moves into
the two-phase region. In the two-phase region the
composition of the liquid and the vapor is not the same.
What is the composition? a. x2 = 0.40 , y2 = 0.60
b. x2 = 0.50 , y2 = 0.70
c. x2 = 0.50 , y2 = 0.50
d. x2 = 0.40 , y2 = 0.70
What is the composition? a. x2 = 0.40 , y2 = 0.60
b. x2 = 0.50 , y2 = 0.70
c. x2 = 0.50 , y2 = 0.50
d. x2 = 0.40 , y2 = 0.70
What is the composition? a. x2 = 0.40 , y2 = 0.60
b. x2 = 0.50 , y2 = 0.70
c. x2 = 0.50 , y2 = 0.50
d. x2 = 0.40 , y2 = 0.70
Boiling in a two component system If we continue to reduce the pressure the system reaches the
boundary with pure vapor.
What is the composition?
a. x2 = 0.40 , y2 = 0.60
b. x2 = 0.50 , y2 = 0.70
c. x2 = 0.50 , y2 = 0.50
d. x2 = 0.40 , y2 = 0.70
What is the composition?
a. x2 = 0.40 , y2 = 0.60
b. x2 = 0.50 , y2 = 0.70
c. x2 = 0.50 , y2 = 0.50
d. x2 = 0.40 , y2 = 0.70
The tie line The tie line shown in Figure (red line) is at a total pressure
of 30 torr. You can read the x2 and y2 values from the plot
(or calculate them using the equations above used to generate
the blue and purple curves in the composition-pressure plot.
The lever rule The tie line can be used to define the quantity of each phase
present in the two phase region. The total composition xa
can be used together with x2 and y2.
za
y2 - za
za
The lever rule
za
y2 - za
za
The lever rule states that the amount of each phase present
is inversely proportional to the length of distance along the
tie line from the phase boundary to the total composition, za.
The lever rule
za
y2 - za
za
The lever rule states:
n liquid
nvapor=
y2 – za
za – x2
The total composition is za.
Non-ideal solutions Many solutions are not ideal. For ideal solutions the role of
intermolecular interactions can be ignored. This may be
because they are small or because two components have
the same interaction with each other that they have with
themselves. In other words similar solvents will form ideal
solutions. However, in many cases, intermolecular interactions
cause deviations from Raoult's law. We can consider the "like"
interactions between molecules of same species and "unlike"
interactions between molecules of different species. If the
unlike-molecule interactions are more attractive than the like
molecule interactions, the vapor pressure above a solution will
be smaller than we would calculate using Raoult's law. If the
unlike-molecule interactions are more repulsive, then the
vapor pressure is greater than for the ideal solution.
Henry’s law The statement of Henry’s law is:
P1 = x1kH,1
It looks like Raoult’s law except that you have this
funny constant kH,1 instead of P1* (the vapor pressure of
component 1). This law is only valid for dilute solutions,
i.e. when component 1 is the solute. Under these conditions
the vapor pressure of component 1 really does not matter,
because component 1 is mostly surrounded by component 2
and so its properties really quite different from the properties
of pure 1.
Henry’s law can be applied to mixtures of solvents
And also to solutions of gases in liquids. For example, see
the problems on the concentration of O2 and N2 in water at
the end of the lecture.
Henry’s law Attractive interactions between unlike molecules leads to
negative deviations from Raoult's law (lower vapor pressure
than ideal) and repulsive interactions lead to positive
deviations (higher vapor pressure than ideal).
As any solution approaches a mole fraction of one (i.e.
approaches a pure solution of one component) it becomes
an ideal solution. In other words, P1 x1P1* as x1 1.
However, as x1 0 the component is surrounded by unlike
molecules and the solution has the maximum deviation from
ideal behavior. For this case we define Henry's law,
P1 x1kH,1 as x1 0. In this expression kH,1 is the Henry's
law constant. Although we have focused on component 1 the
same holds true for component 2.
Non-ideal solutions For the example shown in the plot above we have assumed
that P1* = 100 torr. Note that as x1 1 the slope approaches
the ideal slope obtained from Raoult's law. However, as
x1 0 (and therefore x2 1) the slope is quite different
from ideal behavior. Note that the slope has the value of the
Henry's law constant kH,1. This is depicted in the Figure below
(purple line). The Henry's law value can be quite different from
the ideal value.
Activity The activity in non-ideal solutions corresponds to mole
fraction in ideal solutions.
The activity replaces mole fraction in the expression for the
chemical potential.
When considering a non-ideal solution the above expressions
hold and thus the mole fraction xj is no longer equal to Pj/Pj*.
However, as the mole fraction approaches unity (a pure
substance) the solution becomes ideal.
Thus, as xj 1, aj xj.
a j =Pj
Pj
*
m jsoln = m j
* + RT ln a j
The activity coefficient
We can define an activity coefficient g1 such that
g1 = a1/x1.
The property of the activity coefficient is that it
approaches a value of 1 (ideal behavior) as the
composition approaches the pure solvent:
a1 x1 and g 1 1 as x1 1. Thus, the solution
This definition is based on a Raoult's law standard
state, which is also known as a solvent standard state.
The activities or chemical potentials are meaningless
unless we know the standard state
Henry’s law constant and the
solubility of gases
Henry’s law constants in H2O
(atm x 103)
He 131
N2 86
CO 57
O2 43
Ar 40
CO2 1.6
Problem: Divers get the bends if
bubbles of N2 form in their blood
because they rise too rapidly.
Calculate the molarity of N2 in
water (i.e. blood) at sea level and
100 m below sea level.
At sea level: aN2 = PN2
/kH,N2 = 0.8 atm/86 x 103 atm = 9.3 x 10-6
cN2 = 55.6 aN2
= 5 x 10-4 mol/L
At 100 m: aN2 = PN2
/kH,N2 = 9.8 atm/86 x 103 atm = 1.1 x 10-4
cN2 = 55.6 aN2
= 6 x 10-3 mol/L
A note on conversion from
mole fraction to molarity The conversion from mole fraction to molarity can be
solved analytically.
Note that for water as solvent (component 1) x1~ 1 and the
Concentration of water is c1 ~ 55.6 so that the conversion
For a dilute solute such as a gas is c2 ~ 55.6 x2
x1 =n1
n1 + n2
=c1
c1 + c2
since n1 = c1V and V cancels
x1(c1 + c2) = c1
x1c2 = c1(1 – x1)
x1c2 = c1x2
c2 = c1
x2
x1
Question Henry’s law constants in H2O
(atm x 103)
He 131
N2 86
CO 57
O2 43
Ar 40
CO2 1.6
A species of fish requires a
concentration of O2 > 100 mM.
A marine biologist is trying to
determine the depth profile for O2
in sea water. The first step is to
calculate the concentration of O2
in sea water at sea level.
As an assistant you perform the calculation and find that the
O2 concentration is:
A. 250 mM
B. 430 mM
C. 760 mM
D. 4300 mM
As an assistant you perform the calculation and find that the
O2 concentration is:
A. 250 mM
B. 430 mM
C. 760 mM
D. 4300 mM
Question Henry’s law constants in H2O
(atm x 103)
He 131
N2 86
CO 57
O2 43
Ar 40
CO2 1.6
Most fish require a concentration
of O2 that is greater than 100 mM.
A marine biologist is trying to
determine the depth profile for O2
in sea water. The first step is to
calculate the concentration of O2
in sea water at sea level.
aO2 = PO2
/kH,O2 = 0.2 atm/43 x 103 atm = 4.7 x 10-6
cO2 = 55.6 aO2
= 2.5 x 10-4 mol/L
The Henry’s law constant is
an equilibrium constant Gases dissolve in liquids to form solutions. This dissolution
is an equilibrium process for which an equilibrium constant
can be written. For example, the equilibrium between oxygen
gas and dissolved oxygen in water is O2(aq) <--> O2(g).
The equilibrium constant for this equilibrium is:
K’H = p(O2)/c(O2).
The form of the equilibrium constant shows that the
concentration of a solute gas in a solution is
directly proportional to the partial pressure of that
gas above the solution. The form of the equation can be
Rearranged to give:
p(O2) = c(O2)K’H = x(O2) c(H2O)KH
The Henry’s law constant is
tabulated for c and x The Henry’s law constant can be tabulated for mole fraction
(as seen in the previous problem) or for molarity. If the units
of the Henry’s law constant are atm then it is valid for mole
fraction. If the units are atm/(mol/L) then K’H is tabulated
for molarity. The relationship between the two is:
p(O2) = c(O2)K’H = x(O2) c(H2O)KH
So that K’H = 55.6 (mol/L)KH since the concentration of water
is c(H2O) = 55.55 molar. For example, K’H is 757 atm/(mol/L).
KH =KH
55.6= 757
55.6= 13.6