Diffusion July 2012 - Hansen Solubility Parameters

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DIFFUSION IN POLYMERS

CHARLES M. HANSEN

OUTLINE

 Laws of Diffusion

 Generalized Solutions to these Laws

 Concentration Dependent Coefficients

 Surface Condition can be significant

 Combine These - No Anomalies

 Predict Missing Data from Limited Results

 Control Solvent Retention

FICK’S FIRST AND SECOND LAWS

Law 1: F = - D

0

(

 c/

 x)

For Steady State Flux in the x Direction, and

Law 2:

 c/

 t =

/

 x (D

0

 c/

 x)

This is also called the Diffusion Equation

DIMENSIONLESS VARIABLES

Dimensionless time:

T = D

0 t/L

2

(cm

2

/s)(s/cm

2

)

Dimensionless distance:

X = x/L

Dimensionless concentration:

C = (c – c

0

)/(c

- c

0

)

FOR STEADY STATE PERMEATION

At low concentrations ( ≤1%) D(c) = D

0

F = - D

0

(c

1

– c

2

)/L

For Concentration Dependent Diffusion -

D(c) increases by a factor of 10 for each

3%v increase in concentration (See Below)

MEASURING DIFFUSION

COEFFICIENTS

Half-time (t

½

) equation for measuring D

0

D

0

= 0.049 L

2

/t

½

Corrections required for concentration dependence (M) and surface resistance (B)

D ( c )

F

M

F

B

0 .

049

L

2 t

½

CORRECTIONS FOR CONCENTRATION

DEPENDENCE ALONE

Note huge corrections for desorption

D max

1

2

5

10

1

10

2

10

3

10

4

10

5

10

6

10

7

10

8

Desorption Absorption

(F d

)

1/2

1.00

(F d

)

1/4

1.00

(F a

)

1/2

1.00

1.56

2.70

1.55

2.61

1.30

1.70

4.00

3.84

13.40

10.20

43.30

23.10

2.01

3.30

4.85

138.7

47.40

443.0

89.0

6.14

7.63

1,370.0 160.5

8.97

4,300.0 290.0

10.60

13,670.0 506.0

12.10

F s

SURFACE CONDITION

= -D s

 C s

/  x = h(C eq – C s

)

External Flux at surface, F s

, equals mass transfer coefficient (cm/s) times concentration

2 difference, g/cc giving g/cm s

In dimensionless terms the ratio of diffusion resistance to surface resistance is given by B

Corrections best by curve fitting (See Below).

B = R d

/R s

= (L/D

0

)/(1/h) = hL/D

0

CORRECTIONS FOR SURFACE RESISTANCE

FOR D

0

= CONST.

B = hL/D = R d

/R s

B

10

2

1

0.5

0.1

1/B

0

0.1

0.5

1

2

10

F

B

1.0

1.45

3.14

4.95

6.8

37.5

PERMEATION WITH SURFACE

AND/OR EXTERNAL RESISTANCES

F =

 p/(L/P app

) =

 p/(L/P

+ R

1

+ R

2

+ R

3

…)

L/P app

= L/P

+ R

1

+ R

2

+ R

3

….

1/P app

= 1/P

+ (R

1

+ R

2

+ R

3

….)/L

Use Plot of 1/P

Versus 1/L

TRUE PERMEATION COEFFICIENT (P

BY EXTRAPOLATION (ACRYLIC FILMS)

)

1

P app x 10

-12

20

15

10

5

P 

0 5 10 15 20 25

1 x 10

L

-3

DIFFUSION SIDE EFFECTS

 Film: Thickness (L), length (l), width (w)

D

0

= D app

/(1 + L/l + L/w)

2

 Circular Film: Thickness (b), Radius (R)

D

0

= D app

/(1 + b/R)

2

 For L = 1mm and w = 10mm: D app

/D

0

= 1.21

 Tensile bars (L = 2-4mm, w=10mm): Do not use!

UNIQUE DATA USED IN FOLLOWING

 The system chlorobenzene in poly(vinyl acetate) has been studied extensively with all relevant data reported in my thesis and subsequent journal articles. See the next slides. Absorption data from one equilibrium to another, desorption data from different equilibria to vacuum, and film drying (years) all present a unified and coherent picture of solvent diffusion in polymers, if one accounts for concentration dependence and significant surface effects when present.

D(c) FOR CHLOROBENZENE IN PVAc FOR

ALL CONCENTRATIONS (HANSEN, 1967)

4

6

0.2 Vf ~ 1 decade

Absorption

8

10

0.03 Vf

1 decade

~

Desorption

Absorption

D

APP

12

14

0 0.2

0.4

Vf

Isotope technique

D

C

D

1

(dry film)

0.6

0.8

Selfdiffusion

1.0

DROP IN CURVE ABOVE 0.2 V

f

 When apparent diffusion coefficients are measured by absorption above a break point, the surface condition becomes progressively more important and the apparent diffusion coefficients become lower and lower. Proper interpretation allows these to be corrected to values expected from other measurements.

Initial S-curvature indicates surface resistance is important. The consequences are shown in the following slides.

DESORPTION AND ABSORPTION GIVE SAME

D(c) WITH CORRECTION (HANSEN 1967, 2004)

6

Isotope

8

Absorption F = F x F

B

= 1.3 x 1.25

= 1.63

F = F x F

B

= 1.2 x 250

= 300

10

Desorption

(to vacuum)

12

14

0.1

0.2

0.3

Vf

0.4

0.5

0.6

(F a

ABSORPTION WITH CORRECTIONS

) REQUIRED FOR D(c) AND F

B

FOR R s

Chlorobenzene / polyvinyl acetate

1.0

0.8

L = 118 µm f f

0.6

D = 1.8(10)

-8 cm² sec

B ~ 15

0.4

0.2

0

1 2 3 4 5 t , min ½

6 7 8

ADDITIONAL EXAMPLES OF SURFACE

RESISTANCE – COC POLYMER

(NIELSEN, HANSEN 2005)

Absorption of selected solvents in a COC polymer

1200

300

1000

200

800

100

600

400

0

0 5 10 15 20

Hexane

THF

Diethylether

1,2-Dichloroethylene

200

0

0 20 40 60 80

Sqrt time in min

100 120 140 160

S-SHAPED CURVES CAUSED BY SURFACE

RESISTANCE (NIELSEN, HANSEN 2005)

Absorption of selected solvents in a COC polymer

60

50

40

30

20

10

0

0 50 100 150 200 250 300 350 400

Sqrt time in min

Butylacetate

Ethylacetate

ABSORPTION – CASE II AND SUPER CASE II

CAUSED BY COMBINED ( Hansen, 1980)

R d and R s for D = D

0 e kc

1.0

0.8

0.6

B:

10

9

10

8

10

7

0.4

0.2

0.0

0.0

0.2

0.4

0.6

T x 10

6

0.8

1.0

1.2

10

6

1.4

CONCENTRATION GRADIENTS COMBINED

R d

AND R s

FOR D = D

0 e kc

( Hansen, 1980)

0.4

0.2

0.0

0.0

1.0

0.8

0.6

0.869

0.037

0.098

0.146

0.216

0.125

0.250

0.375

X

0.500

0.319

0.625

0.386

0.467

0.750

0.875

0.562

1.0

DRYING OF A LACQUER FILM

(Hansen, 1967, 1968)

10

1

V

2 = 10

6

V t = 10

10

C

A = 0·2

B as indicated

10

Exptl.

165 microns

10

-1

B=10

6

B=10

7

C

A

Exptl.

22 microns

C

S

= O

For B=10

7

~ M

O

B=10 5

C

S

= O

For B=10

6

C

A

C

S

= O

For B=10

5

Calculated

Experimental

Effect of water - a steeper slope

One day L=30 microns

10

-2

10

-7

10

-6

10

-5

10

-4

T,

D

O t

(L)

2

Dimensionsless

10

-3

10

-2

H

3

H

C

3

C

CH

3

OH

O

O

H

3

C

O

CH

3

CH

3

CH

3

CH

3

CH

3

H

3

C

CH

3

O

CH

3

RELATIVE SOLVENT RETENTION

(HANSEN, 1967)

MOLECULAR SIZE AND SHAPE

Cl

O

H

3

C CH

3

O

N

+

O

Cl

CH

3

O

H

3

C O

H O

O

CH

3

CH

3

O

H

3

C O CH

3

O

CH

3

H

3

C

H

3

C

O

N

+

O

O

O

O

O

H O

CH

3

O

N

+

O

O CH

3

H O

O

CH

3

H

3

C

OH

Effect of Molecular Properties on

Compare Methanol with Iodine

D

0

GENERAL ARTICLE APPEARS EXPLAINING

“ANOMALIES” USING DIFFUSION EQUATION

 Much of the above has been presented in

Chapter 16 of Second Edition of Hansen

Solubility Parameters: A User’s Handbook, CRC

Press, 2007. The following article: Hansen CM.

The significance of the surface condition in solutions to the diffusion equation: explaining

"anomalous" sigmoidal, Case II, and Super Case

II absorption behavior. Eur Polym J

2010;46;651-662 contains the next slides.

SIGNIFICANT SURFACE CONDITION FOR

ABSORPTION OF WATER INTO PVALC FROM

BONE DRY TO 0.748 VOLUME FRACTION

CASE II ABSORPTION WITH LINEAR UPTAKE

WITH LINEAR TIME. THE SURFACE

CONCENTRATION INCREASES SLOWLY

SUPER CASE II WITH SLOWLY INCREASING

RATE OF ABSORPTION WITH TIME.

CONCENTRATION GRADIENTS SHOW A FRONT.

HANSEN IS “EXTRANEOUS”:

PETROPOULOS et.al

Petropoulos JH Sanopoulou M

Papadokostaki KG. Physically insightful modeling of non-Fickian kinetic energy regimes encountered in fundamental studies of isothermal sorption of swelling agents in polymeric media. Eur Polym J 2011;47:2053-

2062.

 Hansen extraneous, challenges included

Hansen cannot explain these data!

Next two slides do explain these data

CALCULATED ABSORPTION CURVE AND GRADIENTS

MATCH EXPERIMENTAL DATA FOR ABSORPTION

PERPENDICULAR TO STRETCH DIRECTION:

METHYLENE CHLORIDE IN CELLULOSE ACETATE.

CALCULATED ABSORPTION CURVE IS PERFECT, FRONT

NOT A SHARP STEP, BUT CLOSE TO EXPERIMENTAL.

METHYLENE CHLORIDE IN STRETCHED CELLULOSE

ACETATE STRETCH DIRECTION.

ARE INITIAL CONDITIONS MAINTAINED?

Thomas and Windle Case II Example

Methanol/PMMA with Iodine Tracer

Straight line absorption with linear time cited as excellent example of

Case II behavior.

This result is duplicated:

Diffusion equation with significant surface effect and exponential D(c)

Thomas and Windle Case II Example

Windle, “Case II Sorption” in Comyn, Polymer Permeability (1985)

Iodine tracer lags methanol in PMMA at 30 °C showing apparent step-like gradient.

Methanol does not have this

“advancing sharp front”.

Iodine tracer far too slow as shown in the next slide.

Methanol gradients become flat at longer time.

Methanol/PMMA Absorption at 30ºC

Calculated Concentration Gradients Flat at 13 hours

Super Case II: n-Hexane/Polystyrene

Hopfenberg and Coworkers

Hopfenberg and Coworkers Super Case II

Correctly Modeled Absorption, D

0

, and h.

CONCLUSION:

STRESS RELAXATION NEED NOT BE INVOKED.

Stress relaxation phenomena need not be invoked to explain the cases examined including Thomas and Windle Case II, Super

Case II, and Sigmoidal examples or the studies of Petropoulos and coworkers.

The diffusion equation seems to fully describe all of these studies when the a significant surface condition is included and exponential diffusion coefficients are used.

DIFFUSION IN POLYMERS

SUMMARY

 Laws of Diffusion

 Generalized Solutions to these Laws

Concentration Dependent Coefficients

Surface Condition involved with ”Anomalies”

 Combine These - No Anomalies

 Predict Missing Data from Limited Results

 Estimate Behavior at Different Conditions

 Improved understanding

Thank you for your attention!

For further contact please visit: www.hansen-solubility.com

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