Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer...
Transcript of Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer...
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1
Polymer Thermodynamics
Prof. Dr. rer. nat. habil. S. Enders
Faculty III for Process ScienceInstitute of Chemical EngineeringDepartment of Thermodynamics
Lecture
0331 L 337
6. Thermodynamics of Polymer Solutions
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2Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.1. Introduction
P = constant
( )
F F I I II II F I IIA A A
F I IF I II I I II II A AA A A II I II
A A
x n x n x n n n n
x x nx n n x n x nx x n
= + = +
−+ = + → =
−
0.0 0.2 0.4 0.6 0.8 1.0250
260
270
280
290
300
310
320
tie line
critical point
meta-stable
meta-stable
stable
stableinstable
spinodalebinodale
T / K
XA
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3Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.1. Introduction
phase equilibrium conditions
1 2
1 2
1 2
L LA AL LB BL LP P P
μ μ
μ μ
=
=
= = S2
T,P=constant
S1II
I
free
mix
ing
enth
alpy
composition
instability limit
2
2
( ) 0MIX g xx
⎛ ⎞∂ Δ=⎜ ⎟∂⎝ ⎠
3
3
( ) 0MIX g xx
⎛ ⎞∂ Δ=⎜ ⎟∂⎝ ⎠
critical conditions
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4Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.1. Introduction
0( , , ) ( , ) ln lni i i i iT P x T P RT x RTμ μ γ= + +
( ) ( )1 1 1 2 2 2
0 0
1 1 2 2 1 1
1 1 2
2 2
2
( , ) ln ln ( , ) ln ln
ln ln ln ln ln ln
L L L L L LA A A A A A
L L L L L L L LA A A
L L L L
A A A
A A A A
A A
T P RT x RT T P RT x RT
x x
x x
x x
μ γ μ γ
γ γ γ γ
γ γ
+ + = + +
+ = + →
=
=
gE-model for the determination of the activity coefficients is necessary
( )( ) ( ) 1E
A B A Ag A T x x A T x xRT
= = −2
2
ln ( )
ln ( )B A
A B
A T x
A T x
γ
γ
=
=i.e.
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5Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.1. Introduction
( ) ( ) ( )
( ) ( ) ( )
1 2 21 2 2 12
1 2 21 2 2 12
ln ( ) 2
ln ( ) 2
LL L L LBB B B BL
B
LL L L LAA A A AL
A
x A T x x x xx
x A T x x x xx
⎛ ⎞ ⎡ ⎤= − +⎜ ⎟ ⎢ ⎥⎣ ⎦⎝ ⎠⎛ ⎞ ⎡ ⎤= − +⎜ ⎟ ⎢ ⎥⎣ ⎦⎝ ⎠
system of equations made from 2 equations → 2 quantities can be calculated
1) T and xAL1→ fixed xA
L2
2) T and xAL2→ fixed xA
L1
3) xAL1 and xA
L2→ fixed T
3 possibilities:
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6Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.1. Introduction
spinodale2
2
( ) 0MIX g xx
⎛ ⎞∂ Δ=⎜ ⎟∂⎝ ⎠
( )
( )2
2
1 1 2 ( ) 0
ln ln ln ln
1 1 2 ( ) 21 1
1 ( )
MIX A A B B A A B B
MIXA A
AA A A A
g RT x x x x x x
g A T x A T xx
Ax x
Tx x
γ γΔ = + + +
⎛ ⎞ ⎛ ⎞∂ Δ= + − − − =⎜ ⎟ ⎜ ⎟∂ −
−⎠ −⎠
+⎝
=⎝
2 2ln ( ) ln ( )B A A BA T x A T xγ γ= =
critical point
( )
3
23 2
( ) 1 1 01
12
CMI
A AA
X g x xx x x
⎛ ⎞∂ Δ= − + = →⎜ ⎟∂ −⎝ ⎠
=
( ) 2 ( ) ( ) spontaneous demixing( ) ( ) stable or metastable
C C
C
A T A T A TA T A T
= > ⇒< ⇒
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7Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
1. Why are polymers usually do not dissolve in normal solvent ?2. Do we have phase separation (LLE) for polymer solutions ?3. How depends phase separation on the molecular weight?
Problems:
Differences between low-molecular weight mixtures and polymer solution
structure of polymer depends on solvent concentration
the structure of both components do not depend on concentration
both components show a big difference in size→ additional parameter molecular weight distribution
both components have approximately the same size
i.e. PS in cyclohexanei.e. benzene + toluene
polymer solutionlow-molecular weight mixture
6.1. Introduction
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8Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Taking into account the differences in size:
division of polymers into segments
standard
ii
LrL
=
Properties1. possibility L= molar volume
disadvantage: volumes depend on temperature2. possibility L = molar mass3. possibility L = degree of polymerization4. possibility L = van der Waals-volume (quantity b in the van der
Waals – equation of state)advantage: available by experiments using X-ray diffraction or by prediction
from molecular data (group-contribution method by Bondi)do not depend on temperature
Lstandard = property of an arbitrarily chosen standard segment (i.e. solvent or monomer unit)
6.1. Introduction
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9Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
division of polymers into segments
standard
ii
LrL
=segment-related thermodynamic quantities(segment-molare quantities)
polymer solution made from solvent (A) + polymer (B)
AA A
A A B B A A B B
r x zx zr x r x r z r z
= ⇒ =+ +
i.e. cyclohexane + polystyrene MPS=100000g/mol xB=0.00001 Lstandard= molar mass of solvent =84.16g/mol-1
100000 / 84.16 /1188.2 184.16 / 84.16 /PS CH
g mol g molr rg mol g mol
= = = =
1188.2*0.00001 0.011741*(1 0.00001) 1188.2*0.00001PSx = =
− +
Taking into account the differences in size:6.1. Introduction
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10Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
the structure of polymer depends on concentration
diluted polymer solutionno entanglements of the polymer chain
semi-diluted polymer solution,entanglements of the polymerchain
overlapping concentration c‘‘
6.1. Introduction
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11Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
vapor pressure of polymer solution
exp. data: B. A. Wolf, et al. University of Mainz, 1995
ideal mixturevery strong
derivation from the behavior of ideal
mixture
?
6.1. Introduction
CH/PS 233
0 0.2 0.4 0.6 0.8 1φPS
4
8
12
16
P [a.u.]
35°C45°C
55°C
65°C
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12Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
phase diagramcyclohexane + PSat different molecular weightsin [kg/mol] of PS
example: MPS=37000 g/molwPS=0,1 T=280 K
Experimental result: demixing
2
2
( )/ 0mix
PS
meta stableg RT spinodale
xinstable
>⎛ ⎞∂ Δ
=⎜ ⎟∂⎝ ⎠ <
6.1. Introduction
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13Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
real low-molecular weight mixture
WWAB≠WWAA≠WWBB
derivations from the behavior of an ideal mixture are caused by intermolecular interaction
model of regular mixtureHildebrand (1933)
The real behavior can be explained completelyby enthalpic effects.
0E E Es g h= → =
AB AA BBWW WW WW=
6.1. Introduction
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14Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Hildebrand model of regular mixtureThe real behavior can be explained completely by enthalpic effects.
0E E Es g h= → =E
A B ABg v DRT
φ φ=
0
01
i
i ik
i ii
x v
x vφ
=
=
∑0
1 10
k kE
i i i ii i
v v x v x v= =
= → = =∑ ∑
( )2A B
ABDRT
δ δ−=
δi solubility parameter
δCH=16.7 (J/cm3)1/2 δPS=17.4 (J/cm3)1/2
( )2
3 3
16.7 17.4 mol0.000218.314 280 cmCHPS
JmolKD
cm J K−
= =
6.1. Introduction
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15Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
E
A B ABg v DRT
φ φ= 3
mol0.00021cmCHPSD =
2 2 20 0
2 3
/ 21 011
Mix AB A B
B B B
g RT D v vx x x v
⎛ ⎞∂ Δ= + −⎜ ⎟∂ −⎠
<⎝
3
3
3 3
111 1.0556
37000 350511.0556
CH PS
PSPS
PS
cm gvmol cm
M g cm cmvmol g mol
ρ
ρ
= =
= = =
Table book:
CH CH PS PSv x v x v= +
example: MPS=37000 g/molwPS=0,1 T=280 K
Hildebrand model of regular mixtureThe real behavior can be explained completely by enthalpic effects.
6.1. Introduction
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16Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
3 3
3
mol0.00021 111 35051cmCHPS CH PS
cm cmD v vmol mol
= = =
2 2 2
2 3
/ 21 1 01
Mix CHPS CH PS
PS PS PS
g RT D v vx x x v
⎛ ⎞∂ Δ= + −⎜ ⎟∂ −⎠
<⎝
CH CH PS PSv x v x v= +
example: MPS=37000 g/mol wPS=0.1 T=280 K
3 2
2
/ 2cm0.00025267 v=119.828m
6o
65l
3.
PS PS PS
PS PS PS PSPS
PS CH PS CH PS CHPS CH
PS CH PS CH PS CH
PMix
PS
S
m w m wn M M Mx m m w m w m w wn n
M M M M M
T
M
gx
x R⎛ ⎞∂ Δ=⎜ ⎟∂⎝ ⎠
= = = =+ + + +
=
conflict to experimental
findings
interaction are not the reasons for the strong real effects
6.1. Introduction
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17Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
real polymer solution
WWAB=WWAA=WWBB
derivation from ideal behaviorcaused by differences in size
model of ideal-athermic mixture
J.P. Flory (1930)M.L. Huggins
The real behavior can be explained completely by entropic effects.
0E E Eh g Ts= → = −
→ Flory-Huggins mixture
6.2. Flory-Huggins Theory
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18Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
WWAB=WWAA=WWBB
model of ideal-athermic mixture
0E E Eh g Ts= → = −
Polymer chains will be arranged on latticesites of equal sizes (i.e. v0A). The number of occupied lattice site dependson segment number r.
Boltzmann’s definition of entropy
lnBS k= Ω
kB Boltzmann’s constantΩ thermodynamic probability
monomer solution
polymer solution
polymer coil
6.2. Flory-Huggins Theory
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19Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Statistical Interpretation of Entropy
ε1
ε2
ε3
Number of possible configuration for 3 distinguishable particles in 3 rooms
P=N! = 3*2*1 = 6
Number of possible configurations corresponds to the permutations of the number of particles:
probability:
1 2 3
!! ! ! !i
NWN N N N
=…
W is called „thermodynamic probability“ and it is the number of possible configuration for a given macroscopic state.
6.2. Flory-Huggins Theory
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20Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Example: distribution of 4 particles with identical energy in 4 volumes.
WC= 4!/(2!1!1!0!)= 4!/2! =12
WA= 4!/(4!0!0!0!)= 4!/4! =1
C
D
A
B WB= 4!/(3!0!1!0!)= 4!/3! =4
WD= 4!/(1!1!1!1!)= 4!/1! =24
The macroscopic state D can be realized by the most configurations.
The macroscopic state D has the highest thermodynamic probability.
6.2. Flory-Huggins Theory
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21Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Model of ideal-athermic mixture
0E E Eh g Ts= → = − lnBS k= Ω
Ω represents the number of distinguishable possibilities of the system to fill the lattice places with particles.
size of the lattice place: v0A
Every lattice place is occupied either with polymer segmentor with a solvent molecule.The polymer segments of a polymer chain are connected bychemical bond and hence they can not move freely.
NA-solvent molecules + NB- polymer chains (every chain consist of r-segments)
number of total lattice places: N0=NA+r*NBevery lattice place is surrounded by q next neighbors (coordination number)
cubic lattice q=6
6.2. Flory-Huggins Theory
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22Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
model of ideal-athermic mixture
0E E Eh g Ts= → = − lnBS k= Ω
( ) 21 0 1 rN q qν −= −the first polymer chain has ν1 possibility to arrange
0 ( 1)fN N i r= − −number of empty lattice places Nf, if the lattice is filled with i-1 polymer chains
the probability to find an empty place is equal to Nf/N0
number of possibilities to arrangefor the chain i: ( )
12
0
1r
rfi f
NN q q
Nν
−−⎛ ⎞
= −⎜ ⎟⎝ ⎠
1
!2
Bi N
ii
rBN
υ=
=
⎡ ⎤⎢ ⎥⎣ ⎦Ω =∏
(1 ) ln(1 ) lnBMix B B B
xs R x x xr
⎡ ⎤Δ = − − − +⎢ ⎥
⎢ ⎥⎣ ⎦
6.2. Flory-Huggins Theory
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23Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
(1 ) ln(1 ) lnBMIX B B B
xg RT x x xr
⎡ ⎤Δ = − − +⎢ ⎥
⎢ ⎥⎣ ⎦
(1 ) ln(1 ) lnBMix B B B
xs R x x xr
⎡ ⎤Δ = − − − +⎢ ⎥
⎢ ⎥⎣ ⎦
( ) ( )( )
( )2
2
/ 1 1ln 1 1 ln
1/ 1 1 10 011 1
MIXB B
B
B BMIX
B
B B B BB
g RT x xr rx
rx xg RT xrx rx x rxx
⎛ ⎞∂Δ⎜ ⎟ = − − − + +⎜ ⎟∂⎝ ⎠
⎛ ⎞ + −∂ Δ⎜ ⎟ = + = → = → = −⎜ ⎟ −− −∂⎝ ⎠
r ³1 negativesegment mole fractionis nonsense
ideal-athermicmixture can not demixed
model of ideal-athermic mixture6.2. Flory-Huggins Theory
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24Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
model of real polymer solutions
(1 ) ln(1 ) ln RBMIX B B B
xg RT x x x gr
⎡ ⎤Δ = − − + +⎢ ⎥
⎢ ⎥⎣ ⎦
Rg description of the derivation of a real polymer solution from anideal-athermic mixture
[ ]12AB A B
B
A B
qk T
ε ε ε ε
εχ
Δ = − +
Δ=
interaction energy between lattice places
χ Flory-Huggin‘s interaction parameter
bad solventχ>0
Ideal - athermic mixtureχ=0
good solventχ<0
0 (1 )R RB Bg h N q x x ε= = − Δ
6.2. Flory-Huggins Theory
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25Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
model of real polymer solutions
(1 ) ln(1 ) ln RBMIX B B B
xg RT x x x gr
⎡ ⎤Δ = − − + +⎢ ⎥
⎢ ⎥⎣ ⎦
0 0(1 ) (1 ) (1 )
B
B
R R BB B B B B B
q k Tk T q
k Tg h N q x x N q x x RT x xq
ε χχ ε
χε χ
Δ= Δ =
= = − Δ = − = −
χ Flory-Huggins interaction parameter
(1 ) ln(1 ) ln (1 )MIX BB B B B B
g xx x x x xRT r
χΔ= − − + + −
Flory-Huggins-equation
6.2. Flory-Huggins Theory
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26Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
(1 ) ln(1 ) ln (1 )MIX BB B B B B
g xx x x x xRT r
χΔ= − − + + −
( ) ( ) ( )
( ) ( )
2
2
3
2 23
/ 1 1ln 1 1 ln 1 2
/ 1 1 2 01
/ 1 1 01
MIXB B B
B
MIX
B BB
MIX
B B B
g RT x x xr rx
g RT
x rxx
g RT
x x r x
χ
χ
⎛ ⎞∂Δ⎜ ⎟ = − − − + + + −⎜ ⎟∂⎝ ⎠⎛ ⎞∂ Δ⎜ ⎟ = + − =⎜ ⎟ −∂⎝ ⎠⎛ ⎞∂ Δ⎜ ⎟ = − =⎜ ⎟∂ −⎝ ⎠
spinodal condition
critical condition
6.2. Flory-Huggins Theory
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27Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
(1 ) ln(1 ) ln (1 )MIX BB B B B B
g xx x x x xRT r
χΔ= − − + + −
( ) ( ) ( ) ( ) ( )
( )( ) ( ) ( ) ( )
( ) ( )( )
3 2 2 2
2 23
2 2
1,2 2
1,2
/ 1 1 0 1 1 21
1 20 1 2 1 01 1
2 4 1 1 1 11 12 1 1 1 1 14 1
0 1 11
11B
MIXB B B B
B B B
BB B
B
c
B
B
g RT r x x x xx x r x
xx r x xr r
rx rr r r r rr
r rxr r
x
⎛ ⎞∂ Δ⎜ ⎟ = − = → = − = − +⎜ ⎟∂ −⎝ ⎠
→ = − + − → = − +− −
±= ± − = ±
− −= =
−
− − =− − − − −−
< <−
→
6.2. Flory-Huggins Theory
![Page 28: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/28.jpg)
28Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0 1000 2000 3000 4000
0,00
0,05
0,10
0,15
0,20
0,25
Flory-Huggins theory
criti
cal c
once
ntra
tion
segment number r
11B c
rxr−
=−
6.2. Flory-Huggins Theory
![Page 29: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/29.jpg)
29Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
(1 ) ln(1 ) ln (1 )MIX BB B B B B
g xx x x x xRT r
χΔ= − − + + −
( )
11 12lim 01 1 2B Bc cr
r rx für r xr r→∞
−= →∞⇒ = = =
−
2
2
/ 1 1 12 0 21 1
0 1/ 2
MIX
B B
C
BB
B
g RT für rx rx xx
x
χ χ
χ
⎛ ⎞∂ Δ⎜ ⎟ = + − = →∞⇒ =⎜ ⎟ − −∂⎝ ⎠
→ ⇒ =0.5
instablespinodalstable
χ>=<for polymers with r →∞
6.2. Flory-Huggins Theory
![Page 30: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/30.jpg)
30Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
1.3725rubber + acetone
0.4425rubber + benzene
0.2820rubber + CCl4
0.1526PVC + THF
0.4425polystyrene + toluene
0.525polyisobutylene + benzene
0.2725cellulose nitrate + acetonecT [°C]system
Flory-Huggins parameter for polymer + solvent - systems
6.2. Flory-Huggins Theory
![Page 31: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/31.jpg)
31Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
B. A. Wolf, University of Mainz, 1995
χ can also depends on polymer concentrationand molecular weight
conflict to FH-theory
6.2. Flory-Huggins Theory
χ
0.0
0.2
0.4
0.6
0.8
1
φPVME
0.0 0.2 0.4 0.6 0.8 1
CH/PVME
MW [kg/mol]
81 51
28
T = 65°C
![Page 32: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/32.jpg)
32Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
B. A. Wolf, University of Mainz, 1995
6.2. Flory-Huggins Theory
χ
0.4
0.5
0.6
0.7
0.8
0.9
0.2 0.4 0.6 0.8
TL / PDMS 170
T=35°C
T=45°C
T=55°C
wPDMS
![Page 33: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/33.jpg)
33Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
formal division of χ in a enthalpic- and a entropic part
( )
22
2
H S
S
H
h Ts h sRT RT R
s hh RT
R T RT T
RTh T TRT RT T
χ χ χ χ
χ χχ
χ
χ χ χ
χ χχ
χχχ
−= + = = −
∂ ∂⎛ ⎞ ⎛ ⎞= − = − → = −⎜ ⎟ ⎜ ⎟∂ ∂⎝ ⎠ ⎝ ⎠∂⎛ ⎞− ⎜ ⎟ ∂∂ ⎛ ⎞⎝ ⎠= = = − ⎜ ⎟∂⎝ ⎠
temperature dependence of χ available
special case: 0H Sχ χ χ− = ⇒ = pseudo-ideal state = Theta-state
1H S
h s h hs s
RT R R T Tχ χ χ χ
χ χχ χ χ⎛ ⎞
= + = − = − ⇒ =⎜ ⎟⎝ ⎠
Theta-temperature
6.2. Flory-Huggins Theory
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34Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0.2
0.03
0.03
0.03
0.04
-0.02
-0.08
cH
0.310.51m-xylole
0.450.48Acetone
0.420.45toluene
0.420.45THF
0.390.43dioxane
0.450.43benzene
0.440.36chloroform
cScsolvent
Flory-Huggins parameter for PMMA + solvent systems
entropic effectsare more importantthan enthalpic effects
6.2. Flory-Huggins Theory
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35Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
B. A. Wolf, Universität Mainz, 1995
6.2. Flory-Huggins Theory
c
fPDMS
0.2 0.4 0.6 0.8-3
-2
-1
0
1
2
3
4
cS
cH
TL/PDMS 170T = 35°C
![Page 36: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/36.jpg)
36Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ
Cohesive Energy eCoh: internal energy of the material if all of its intermolecularforces are eliminated
solubility parameter δ1/ 2
3/ 2cohe Jv mol
δ δ⎡ ⎤
= ⎢ ⎥⎣ ⎦
solubility of polymer P in solvent S ( )2P Sδ δ− has to be small,
as small as possible
( ) ( )22
(1 ) (1 ) BR
BB B B
AAB
h x x xvRT
xRT vRT
δ δχχ
δ δ−=
⎡ ⎤−= − ≈ − →⎢ ⎥
⎢ ⎥⎣ ⎦
2
(298 )CohFe
v K= F molar attraction constant
v molar volume
![Page 37: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/37.jpg)
37Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ example: solubility of polystyrene at 25°CFirst step: Calculation of atomic indices δ and valence atomic δV
Second step: Calculation of connectivity indicesV V V
ij i j ij i jβ δ δ β δ δ= =
0 0 1 1
0 0 1 1
1 1 1 1
5.3973 4.6712 3.9663 3.0159
V V
V Vvertices vertices edges edges
V V
χ χ χ χδ βδ β
χ χ χ χ
≡ ≡ ≡ ≡
= = = =
∑ ∑ ∑ ∑
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38Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ example: solubility of polystyrene at 25°CFourth step: Calculation of molar volume
1.42 0.15Wg
Tv vT
⎛ ⎞⎛ ⎞= +⎜ ⎟⎜ ⎟⎜ ⎟⎜ ⎟⎝ ⎠⎝ ⎠
( )
( )
30 1
3 3
3.861803* 13.748435*
3.861803*5.3973 13.748435*3.0159 62.31
VW
cmvmol
cm cmmol mol
χ χ= +
= + =
Tg=373.15K
3 329862.31 1.42 0.15 95.95373
cm K cmvmol K mol
⎛ ⎞⎛ ⎞= + =⎜ ⎟⎜ ⎟⎝ ⎠⎝ ⎠
![Page 39: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/39.jpg)
39Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ example: solubility of polystyrene at 25°CThird step: Calculation of molar attraction constant F
( )( )( )
( )( )( )
0 0 1 1 3
2
3
2
3
2
97.95 2
134.61
97.95 5.3973 2 4.6712 3.9663 3.0159
134.61 0 0 0
1754.2
V V
Si Br Cyc
Jcmwhere FmolN N N
JcmFmol
JcmFmol
χ χ χ χ⎡ ⎤− + + +⎢ ⎥=⎢ ⎥+ − −⎣ ⎦
⎡ ⎤− + + += ⎢ ⎥
+ − −⎢ ⎥⎣ ⎦
=
![Page 40: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/40.jpg)
40Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ example: solubility of polystyreneFifth step: Calculation cohesive energy eCoh
( )
2
3 3
2
2 3
2 3
(298 )
1754.2 95.95
1754.232.07
95.95
Coh
Coh
Fev K
Jcm cmF vmol mol
Jcm mol kJemol cm mol
=
= =
= =
3 3
32.07 18.2895.95
cohe kJmol Jv mol cm cm
δ = = =
Sixth step: Calculation of solubility parameter δ
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41Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Prediction of χ example: solubility of polystyrene
Seventh step: Calculation of interaction parameter χ( )2
B A
vRTδ δ
χ−
=
4,96690,17690,00300,00050,4520
χ solvent qualityδA [J/cm3]solvent
poor-LLE29,60methanolgood20,42dioxane
excellent18,56benzeneexcellent18,17toluenemiddle14,86n-hexane
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42Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
Application of Flory-Huggins Theory to LLEphase equilibrium conditions
low molecular weight mixtures polymer solutions1 2
1 2
1 2
L LA AL LB BL LP P P
μ μ
μ μ
=
=
= =
1 2
1 2
1 2
L LA A
L LB BL LP P P
μ μ
μ μ
=
=
= =
(1 ) ln(1 ) ln (1 )MIX BB B B B B
g xx x x x xRT r
χΔ= − − + + −
0 0 0 0
, , A
A BB MIX A B MIXA B
B T P n
G G G G G n g n g n gn
μ⎛ ⎞∂⎜ ⎟= → = + + Δ = + + Δ⎜ ⎟∂⎝ ⎠
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43Polymer Thermodynamics6. Thermodynamics of Polymer Solutions
6.2. Flory-Huggins Theory
( ) ( )
( ) ( )
( ) ( )
0 0
2
0
, ,
0
2
,
0
,
(1 ) ln(1 ) ln (1 )
1ln 1
1 1l
1/ / ln 1
n 1
B
A
BA B B B B B BA B
A A B BA
A T P n
B B A AB
B T P n
AA A B B
xG n g n g RT n x x x x xr
G g RT x x xrn
G g RT x x xr
RT RT x x x
n
r
r
μ μ
χ
μ χ
μ
χ
⎡ ⎤= + + − − + + −⎢ ⎥
⎢ ⎥⎣ ⎦⎛ ⎞∂ ⎛ ⎞⎛ ⎞⎜ ⎟= = + + − +⎜ ⎟⎜ ⎟⎜ ⎟ ⎝ ⎠⎝ ⎠∂⎝ ⎠
⎛ ⎞∂ ⎛ ⎞⎜ ⎟= = + − − +⎜ ⎟⎜ ⎟ ⎝ ⎠∂
⎛ ⎞= + + +⎜⎝ ⎠
⎝ ⎠
− ⎟
( ) ( )2
0
2
1 1/ / ln 1BB B A ART RT x x xr r
μ μ χ
χ
⎛ ⎞
⎡ ⎤⎢ ⎥⎣ ⎦
= + − − +⎜ ⎟⎝ ⎠
Application of Flory-Huggins Theory to LLE
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44Polymer Thermodynamics6. Thermodynamics of Polymer Solutions
6.2. Flory-Huggins Theory
10LA
RTμ ( ) ( )2 2
1 1 1 01ln 1L
L L L AA B Bx x x
r RTμχ⎛ ⎞+ + − + =⎜ ⎟
⎝ ⎠ ( ) ( )( ) ( ) ( )
22 2 2
1
2 212 2 1
2
0
1
1ln 1
1ln 1L
L L L LAB B B B
L
L L LB
A
A B
LB
x x x x xrx
x x xr
RT
χ
χ
μ
⎛ ⎞ ⎛ ⎞⎛ ⎞⎜ ⎟ = − − + −⎜ ⎟⎜ ⎟⎜ ⎟ ⎝ ⎠ ⎝ ⎠
⎛ ⎞+ + − +⎜ ⎟⎝ ⎠
⎝→
⎠
( ) ( )2 21 1 1 01 1ln 1
LL L L BB A Ax x x
r r RTμχ⎛ ⎞+ − − + =⎜ ⎟
⎝ ⎠ ( ) ( )( ) ( ) ( )
22 2
2 211 2
2
2 1
2
1 1ln 1
1 11
L L LB A A
LL L L LBA A A A
LB
x x x x xr rx
x x xr r
χ
χ⎛ ⎞ ⎛ ⎞⎛ ⎞⎜
⎛ ⎞+ − − +⎜ ⎟⎝ ⎠
→ ⎟ = − − + −⎜ ⎟⎜ ⎟⎜ ⎟ ⎝ ⎠ ⎝ ⎠⎝ ⎠
Application of Flory-Huggins Theory to LLE
2 equations and 3 unknowns → select one concentration in one phase→ calculation of the concentration in the other phase and the parameter χ using
both equations, where a numerical procedure must be appliedor reduce the system of equations to one equation
equation 1
equation 2
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45Polymer Thermodynamics6. Thermodynamics of Polymer Solutions
6.2. Flory-Huggins Theory
( )( ) ( )
( )( ) ( )
1 12 1 1 2
2 2
2 2 2 22 1 2 1
1 1 1ln 1 1L L
L L L LA BB B A A
L LA B
L L L LB B A A
x xx x x xr r rx x
x x x x
⎛ ⎞ ⎛ ⎞⎛ ⎞ ⎛ ⎞⎜ ⎟ ⎜ ⎟− − − − − −⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠⎝ ⎠ ⎝ ⎠=⎛ ⎞ ⎛ ⎞
− −⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠
Application of Flory-Huggins Theory to LLE
reduce the system of equations to one equation → rearrangement of both equationsaccording χ → to equate both results
from equation 1 from equation 2
equation 3
Now: solve equation 3 in order to calculate the unknown concentration usingroot-searching method, like Newton-Procedurecalculate χ using equation 1 or equation 2
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46Polymer Thermodynamics6. Thermodynamics of Polymer Solutions
6.2. Flory-Huggins TheoryApplication of Flory-Huggins Theory to LLE
321 2( )T
T Tββχ β= + +
special cases:β3=0 only one critical point can be calculated
β2>0 UCSTβ2<0 LCST
β3≠0 two critical points can be calculatedclosed miscibility gap or UCST+LCST
T / K
XA
UCST
XA
T/K
LCST
T / K
XA
XA
T [K
]
![Page 47: Lecture - Institut Prozess- & Verfahrenstechnik: Thermodynamik … · 2009-04-17 · 1 Polymer Thermodynamics Prof. Dr. rer. nat. habil. S. Enders Faculty III for Process Science](https://reader031.fdocuments.us/reader031/viewer/2022031507/5c9ab5c209d3f272758c4ac8/html5/thumbnails/47.jpg)
47Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0 5 10 15 20 25
30
40
50
60
70
80
χ(T)=1.186-207.87/T
MW=500 kg/mol
PAA + Dioxan
T / °
C
wPAA [%]
6.2. Flory-Huggins Theory
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48Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
vapor pressure of polymer solutions
liquid mixture (A+B) « pure vapor phase (A)
solvent A + solute B PBVL ≈ 0
equilibrium condition: ( , , ) ( , )L VA A Ad T P x d T Pμ μ= T = constant
0 0
0
00
1V L L VVL
V VA A A A AA AVL V
A A A
VLL L LA A AVL
A
ideal gas
a xP with
P a
P
xP
ϕ γ ϕ ϕ ϕϕ ϕ
γ
= = =
=
=
→ =
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49Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions6.2. Flory-Huggins Theory
vapor pressure of polymer solutions
0
VLLAVL
A
P aP
=application to polymer solution
( ) ( )2
01ln 1AA A B BRT x x xr
μ μ χ⎡ ⎤⎛ ⎞= + + − +⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦
low-molecular weight mixtures0( , , ) ( , ) lni i i iT P x T P RT aμ μ= +
solvent in polymer solution
( ) ( )( ) ( )
2
2
0
1ln ln 1
1ln ln 1
LA A B B
VL
A B BVLA
a x x xr
P x x xP r
χ
χ
⎛ ⎞⎛ ⎞ = + − +⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠⎛ ⎞ ⎛ ⎞→ = + − +⎜ ⎟ ⎜ ⎟
⎝ ⎠⎝ ⎠possibility to determine χ from experimental data, like vapor pressure of polymer solutions
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50Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
vapor pressure of polymer solutions
liquid mixture (A+B) « pure vapor phase (A)
solvent A + solute B PBVL ≈ 0
equilibria condition: ( , , ) ( , )L VA A Ad T P x d T Pμ μ= T = constant
0 0
0
00
1V L L VVL
V VA A A A AA AVL V
A A A
VLL L LA A AVL
A
ideal gas
a xP with
P a
P
xP
ϕ γ ϕ ϕ ϕϕ ϕ
γ
= = =
=
=
→ =
( ) ( )2
0
1ln ln 1VL
A B BVLA
P x x xP r
χ⎛ ⎞ ⎛ ⎞= + − +⎜ ⎟ ⎜ ⎟
⎝ ⎠⎝ ⎠
Flory-Huggins theory
6.2. Flory-Huggins Theory
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51Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
vapor pressure of polymer solutions
0,0 0,2 0,4 0,6 0,8 1,00
5
10
15
20
T = 298K
r=1 χ=0 ideal mixture r=100 χ=0 ideal-athermic mixture r=100 χ=0.452 real mixture
PS + n-hexanePVL
[kPa
]
segment mole fraction of PS
6.2. Flory-Huggins Theory
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52Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
measurement of χ: inverse gas chromatography (IGC)IGC refers to the characterization of the chromatographic stationary phase (polymer)using a known amount of mobile phase (solvent).The stationary phase is prepared by coating an inert support with polymer and packingthe coated particles into a conventional gas chromatography column.The activity of the given solvent can be related to its retention time on the column.
→ infinity dilution regarding to the solvent
experimental information: N R GV V V= −VR retention volume [m3]VG gas holdup [m3]VN net retention volume [m3]
0NV net retention volume extrapolated to zero column pressure
00
NL GAL G L
A
Vn VkV n V
= = at infinity dilution: A AA A
A A
Pax xγ ϕ
∞ ∞
∞ ⎛ ⎞ ⎛ ⎞= =⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠
fugacity coefficient =1
0
LA A A
A NA A
P x P RTnax x V
∞ ∞
∞ ⎛ ⎞ ⎛ ⎞= = =⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠
6.2. Flory-Huggins Theory
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53Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
experimental estimation of χ shows −χ depends on temperature−χ depends on polymer concentration−χ depends on molecular weight
more complex models are needed
321 2( )T
T Tββχ β= + +
6.2. Flory-Huggins Theory
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54Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Flory-Krigbaum Model (1950): a diluted polymer solution is considered as adispersion of clouds consisting of polymer segments surrounded byregions of pure solvent
( ) ( ) ( )( )2
1 11ln ln 1A A B Ba x x xr
κ ψ⎛ ⎞= + − + −⎜ ⎟⎝ ⎠
enthalpic parameter entropic parameter
1
1
T Theta Temperatureκθ θψ
= = −
Difficulty: the interaction parameter depends not on concentration
6.3. Extensions of Flory-Huggins Theory
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55Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
( )(1 ) ,B BR
Bg RT x x Txχ= −
1. Possibility: ( ) ( )2
0 1 2, ( ) ( ) ( ) ...B B Bx T T T x T xχ χ χ χ= + + + +
advantage: very flexibledisadvantage: empirical, a lot of parameters
2. Possibility: ( ) ( ),1
B
B
Tx Tx
βχγ
=−
advantage: very flexible, semi-empiricaleasy parameter fitting procedure using the critical point
Koningsveld-Kleintjens-Eq.
6.3. Extensions of Flory-Huggins Theory
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56Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0,00 0,02 0,04 0,06 0,08 0,10287,5
288,0
288,5
289,0
289,5
290,0
290,5
TD/PMMA 1770
γ = 0.32281 β1 = 0.24844 β2 = 143.307 / K
T/K
wPMMA
( ) ( ),1
B
B
Tx Tx
βχγ
=−
6.3. Extensions of Flory-Huggins Theory
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57Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
M. Schnell, S. Stryuk, B.A. Wolf, Ind. Eng. Chem. Res. 43 (2004) 2852.
high-pressure production of PE
equation of state is necessary
6.3. Extensions of Flory-Huggins Theory
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58Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Flory-Equation of State
Starting point: partition function
( ) ( )31/3* 1 exprncrnc
combrncZ Z gv vvT
⎛ ⎞= − ⎜ ⎟⎝ ⎠
combinatory factor Zcomb geometrical factor g characteristic volume v*
3rnc = total number of degrees of freedom ( r = segment-number, n = number of molecules, c = mean number of external degrees per segment)
* * *v Tv T P
PP
v T= = =
v*, T* and P* are characteristic quantities = parameters of the polymer
6.3. Extensions of Flory-Huggins Theory
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59Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Flory-Equation of StateStarting point: partition function
( ) ( )31/3* 1 exprncrnc
combrncZ Z gv vvT
⎛ ⎞= − ⎜ ⎟⎝ ⎠
6.3. Extensions of Flory-Huggins Theory
ln
T
ZP kTV
∂⎛ ⎞= ⎜ ⎟∂⎝ ⎠
from statistical thermodynamics:
1/3
1/3
11
Pv vT v Tv
= −−
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60Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Flory-Equation of State
6.3. Extensions of Flory-Huggins Theory
chemical potential for solvent:
1/3* ** *1 1 1
1 1 2 1 1 1* 1/31
22
2
12 1 1 1ln 1 3 ln1
Xv v vRT v P Tv v v v v
μ φ θφ⎡ ⎤⎡ ⎤ ⎛ ⎞⎛ ⎞ −
Δ = + − + + + −⎢ ⎥⎜ ⎟⎢ ⎥⎜ ⎟ −⎢ ⎥⎝ ⎠ ⎝ ⎠⎣ ⎦ ⎣ ⎦
Flory-Huggins term
binary parameters
free volume terminteraction term
1/3* ** *2 2 2
2 2 1 2 2 2* 1/32
21
1
12 1 1 1ln 1 3 ln1
Xv v vRT v P Tv v v v v
μ φ θφ⎡ ⎤⎡ ⎤ ⎛ ⎞⎛ ⎞ −
Δ = + − + + + −⎢ ⎥⎜ ⎟⎢ ⎥⎜ ⎟ −⎢ ⎥⎝ ⎠ ⎝ ⎠⎣ ⎦ ⎣ ⎦
chemical potential for polymer:
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61Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
Flory-Equation of State
6.3. Extensions of Flory-Huggins Theory
calculation of the mixing volume1 1 2 21E v vv v
vφ φ+⎡ ⎤= −⎢ ⎥⎣ ⎦
other equations of state useful in polymer thermodynamics
Sanchez-Lacombe Equation of state (SL-EOS)lattice theory, which allows additionally empty sites
Statistical associated fluid theory (SAFT-EOS)takes into account additionally specific interactions like hydrogen bonding
and associationPerturbed-Chain Statistical associated fluid theory (PC-SAFT-EOS)
further development of SAFT-EOS, takes the chain connectivity into account
( )2
1 1/ 1ln1
rP VT V V V T
−= − −
−
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62Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
6.3. Extensions of Flory-Huggins Theory
Polydispersity effects
three liquid phases for the system polyethylene + diphenyletherat constant temperature and pressure ???
R. Koningsveld, W.H. Stockmayer, E. Nies,Polymer Phase Diagrams, Oxford University Press, 2001
Gibbs ‘s phase rule: F = K – Ph + 2binary system: K=2 F=4-Phfixed P,T: F=2 ® PhMax=2
polymer solutions arenot binary systems
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63Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0,00 0,02 0,04 0,06 0,08 0,10 0,12 0,14 0,16 0,18 0,20295
300
305
310
315
320
T / K
X Ensemble
critical point
spinodal
cloud-point curve
shadow-curve
coexisting curve
6.3. Extensions of Flory-Huggins TheoryPolydispersity effects
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64Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0 200 400 600 800 1000 1200 1400 1600 1800 20000
5
10
15
20
25
30
Feed Phase I Phase II
103 W
(r)
r
fractionation effectPolydispersity effects
6.3. Extensions of Flory-Huggins Theory
phase Ipolymers withhigher chain lengths
phase IIpolymers withlower chain lengths
In both phasesare different polymers.
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65Polymer Thermodynamics6. Thermodynamics of Polymer Solutions
6.4. Swelling Equilibria
solvent
polymer network
V/V00.2 0.5 1 2
T [°C]
20
30
40
50
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66Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
6.4. Swelling Equilibria
Application to drug-delivery systems
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67Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
T = constant
polymer gelP1
P2liquid phase
+
+
+
+
--
- -+
+-
-
''' ''ln ( , ', ') ln ( , '', '') i eli i
T
v Fa T P n a T P nRT V
∂Δ⎛ ⎞= + ⎜ ⎟∂⎝ ⎠
MIX
MIX
el
deformed relaxed
FF F
F FF
Δ = Δ += Δ +
Δ−
ΔelF elastic free energy (deformation of rubber, rubber elasticity)
i.e. Flory-Huggins-theory
2/3
10
1el F VCRT V
⎡ ⎤⎛ ⎞Δ ⎢ ⎥= −⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦
6.4. Swelling Equilibria
first approximation
more information available: G. Maurer, J.M. Prausnitz, Fluid Phase Equilibria 115 (1996) 13-133.
C1 – fit parameterV volume of swollen networkV0 volume of non-swollen network
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68Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
starting point:Li
Si ff = phase equilibrium condition
iso-fugacity criteria
Li0
Li
Li
Li fxf γ=liquid phase:
Si0
Si
Si
Si fxf γ=solid phase:
00 0
0
L S SL L L S S S i i ii i i i i i S L L
i i i
f xx f x ff x
γγ γγ
= → =
Calculation of pure-component properties
0 00 0 0 0
00 0 0
0
( , ) ln ( , ) ln
ln
S LS id L idi ii i i i
LL S i
LS i i i Si
f fg g T P RT g g T P RTP P
fg g g RTf
= + = +
→ Δ = − =
6.5. Solid-Liquid Equilibria
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69Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
0
0
L S Si i iS L Li i i
f xf x
γγ
=0
0 0 0 00
00 0 0
00 0
0
ln
1
1ln
Li
LS i LS i LS i LS iSi
LS iLS i LS i LS iLS LS
LS iL LSi LS iSi
fg RT g h T sf
h Tg h T hT T
Thf g Tf RT RT
Δ = Δ = Δ − Δ
Δ ⎛ ⎞Δ = Δ − = Δ −⎜ ⎟⎝ ⎠
⎛ ⎞Δ −⎜ ⎟Δ ⎝ ⎠= =
0 1ln
LS i S SLSi iL Li i
ThxT
RT xγγ
⎛ ⎞Δ −⎜ ⎟ ⎛ ⎞⎝ ⎠ = ⎜ ⎟⎝ ⎠
SLE for binary systems
6.5. Solid-Liquid Equilibria
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70Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
solids are pure-components 1S Si ix γ =
0
0
ln 1L L LS ii i LS
i
h TxRT T
γ⎛ ⎞Δ
= − −⎜ ⎟⎝ ⎠
SLE
Application to polymer solution using Flory-Huggins theory
( )
0
0
20
0
ln 1 ln
ln 1
L LLS iB BLS
i
L LLS iB ALS
i
h TxRT T
h Tx xRT T
γ
χ
⎛ ⎞Δ= − − −⎜ ⎟
⎝ ⎠
⎛ ⎞Δ= − − −⎜ ⎟
⎝ ⎠
6.5. Solid-Liquid Equilibria
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71Polymer Thermodynamics
6. Thermodynamics of Polymer Solutions
solvent1) xylene only SLE2) amyl acetate or nitrobenzene
A-B SLEC-B LLEor eutectic mixture
6.5. Solid-Liquid EquilibriaT[°C]
80
100
120
140
160
180
200
0.2 0.4 0.6 0.8 wPE
xylene
amylacetate
nitrobenzene
AB
B
C
C