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Polymers in SolutionChapter 10

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(1)

Polymers in Solution

Chapter 10

(2)

Ch 10 Sl 2

Solution thermodynamics

solution = mixing solvent (1) and solute (2)

∆G

m

= G

12

– (G

1

+ G

2

)

∆G

m

= ∆H

m

– T ∆S

m

∆S

m

> 0 always

∆H

m

> 0 almost always

“like dissolves like”

∆Hm = 0 at best (when solute is the same to solvent)

if not, ∆Hm > 0

∆Hm < 0 only when specific interaction like H-bonding exists

For solution, ∆H

m

< T ∆S

m

G12 < (G1 + G2)

(3)

Ch 10 Sl 3

Solubility parameter  ∆H m

∆H

m

= V

m

[(∆E

1

/V

1

)

½

– (∆E

2

/V

2

)

½

]

2

φ

1

φ

2

= V

m

1

– δ

2

]

2

φ

1

φ

2

φ ~ volume fraction

∆E ~ cohesive energy ~ energy change for vaporization

∆E = ∆Hvap – P∆V ≈ ∆Hvap – RT [J]

∆E/V ~ cohesive energy density

[J/cm3 = MPa]

δ ~ solubility parameter

[MPa½] = [(J/cm3)½] ≈ [(1/2)(cal/cm3)½]

δ (∆E, CED) depends on intermolecular interaction

dispersion force

polar interaction

H-bonding

Eqn (10.58) p250

(4)

Ch 10 Sl 4

For solution,

∆H

m

< T ∆S

m

without specific interaction

δ1 = δ2  ∆Hm = 0  ∆Gm < 0

∆δ < 20 MPa½ for solvent/solvent solution

∆δ < 2 MPa½ for solvent/polymer solution

Why? smaller ∆Sm

∆δ ≈ 0 for polymer/polymer solution

(5)

Ch 10 Sl 5

PP soluble in cx? No.

Semicrystalline polymers are not soluble at RT.

positive ∆Hfusion  ∆Hfusion + ∆Hm > T ∆Sm

soluble at higher temperature ~ PP in p-xylene at above 100 °C

solubilize using specific interaction ~ PET in formic acid (H-bonding)

for amorphous state at 25 ºC

(6)

Ch 10 Sl 6

ideal solution ~ ∆H

m

= 0

size of 1 and 2 the same

interaction energy, h

1-1

= h

2-2

= h

1-2

∆G

m

of ideal solution

∆G

1

= µ

1

– µ

1o

= RT ln X

1

∆G

2

= µ

2

– µ

2o

= RT ln X

2

∆G

m

= n

1

∆G

1

+ n

2

∆G

2

= RT (n

1

ln X

1

+ n

2

ln X

2

)

∆S

m

of ideal solution

∆H

m

= 0 

∆Sm = – R (n1 ln X1 + n2 ln X2)

µ ~ chemical potential n ~ number of moles X ~ mole fraction X1 = n1/(n1+n2)

Ideal solution

(7)

Ch 10 Sl 7

∆S m from statistical thermodynamics

lattice model

filling N

1

and N

2

molecules in N

1

+N

2

=N

0

cells

volume of 1 ≈ volume of 2 (for small molecules)

Boltzmann relation, S = k ln Ω

S ~ combinatorial [configurational] entropy

Ω ~ number of (distinguishable) ways

= S

12

– S

1

– S

2

S1 = k ln Ω1 = k ln (N1!/N1!) = 0 = S2

S12 = k ln Ω12 = k ln [(N1+N2)!/N1!N2!]

Fig 10.1 p230

(8)

Ch 10 Sl 8

∆S m of polymer solution

developed by Flory and Huggins

lattice model

filling N

1

solvents and N

2

polymers in N

1

+ xN

2

= N

0

cells

volume of 1 << volume of 2 (by x; x ~ deg of polym’n)

∆S

m

= S

12

– S

1

– S

2

= k ln [Ω

12

/Ω

1

2

] = k ln [Ω

12

/Ω

2

]

1 = 0; Ω2 ≠ 0 (connected)

x (mol wt ) 

n2

 ∆S

m

for polymer/polymer soln,

∆S

m

even smaller (n

1

& n

2

)

n ~ number of moles φ ~ volume fraction φ1 = N1/(N1+xN2)

pp239-243 for derivation

(9)

Ch 10 Sl 9

∆H m

∆G

m

= ∆H

m

– T ∆S

m

in original F-H theory

∆H

m

= N

1

z X

2

[h

12

– ½(h

11

+h

22

)]

= kT N

1

φ

2

χ

modified  entropy change with interaction

χ ~ (F-H polymer-solvent) interaction parameter

χ   ∆Hm   solvent power 

∆Hm = Vm1 – δ2]2

φ

1

φ

2

χ = χ1 = χ12 χ = χH + χS

(10)

Ch 10 Sl 10

Flory-Huggins equation

∆G

m

= ∆H

m

– T ∆S

m

F-H theory predicts polymer solution property,

solubility, miscibility, phase separation, fractionation, ---

vapor pressure, boiling point, ---

but not that precisely.

due to drawbacks of theory like

no volume change, self-intersection, changing χ

especially for dilute polymer solution

Chains are separated in dilute soln.

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