Below you will find several tables (click the tabs) on diffusion, solubility, permeability, chemical resistance and mechanical retention of some commonly used polymers and metals. This selection is based on interesting and popular threads on the forum. If you are interested in an industrial application of the tabled figures, you might take a look at cases. |
Conditions |
System Temperature: |
25 degrees Celsius |
| System Pressure: |
1 Bar |
| Activity of Permeant |
100% |
| |
Material |
Permeant |
Solubility |
D0* |
D|** |
Permeability |
[-] |
[-] |
m3stp / m3 x bar |
m2/ s |
m2/ s |
[m3stp / m3] x [m2 / s] |
gram / m s |
Epoxy Resin |
H2 |
0.1 |
1 10-11 |
1 10-11 |
1 10-12 |
9 10-11 |
| |
|
|
|
|
|
|
Butyl Rubber
(Poly Isobutylene)
|
CO2 |
0.67 |
5.8 10-12 |
5.8 10-12 |
3.9 10-12 |
7.9 10-9 |
O2 |
0.12 |
8.1 10-12 |
8.1 10-12 |
9.7 10-13 |
1.4 10-9 |
N2 |
0.054 |
4.5 10-12 |
4.5 10-12 |
2.4 10-13 |
3.0 10-10 |
H2 |
0.035 |
1.5 10-10 |
1.5 10-10 |
5.3 10-12 |
4.7 10-10 |
| |
|
|
|
|
|
|
PET (Poly Ethylene Terephthalate) ~100% crystalline
|
CO2 |
1.4 |
5.4 10-14 |
6 10-14 |
8 10-14 |
2 10-10 |
O2 |
0.091 |
5.6 10-13 |
5.6 10-13 |
5.1 10-14 |
7.2 10-11 |
N2 |
0.032 |
1.4 10-13 |
1.4 10-13 |
3.6 10-15 |
4.4 10-12 |
H2 |
0.081 |
8.0 10-12 |
8.0 10-12 |
6.4 10-13 |
5.7 10-11 |
| |
|
|
|
|
|
|
HDPE (High Density Poly Ethylene) |
CO2 |
0.29 |
1.2 10-11 |
1.2 10-11 |
3.5 10-12 |
6.8 10-9 |
O2 |
0.046 |
1.7 10-11 |
1.7 10-11 |
7.8 10-13 |
1.1 10-9 |
N2 |
0.025 |
9.3 10-12 |
9.3 10-12 |
2.3 10-13 |
2.8 10-10 |
H2 |
0.073 |
2.6 10-11 |
2.6 10-11 |
1.9 10-12 |
1.7 10-10 |
| |
|
|
|
|
|
|
LDPE (Low Density Poly Ethylene) |
CO2 |
0.25 |
3.7 10-11 |
3.7 10-11 |
9.4 10-12 |
1.8 10-8 |
O2 |
0.050 |
4.6 10-11 |
4.6 10-11 |
2.3 10-12 |
3.2 10-9 |
N2 |
0.021 |
3.2 10-11 |
3.2 10-11 |
6.4 10-13 |
7.9 10-10 |
H2 |
0.16 |
4.7 10-11 |
4.7 10-11 |
7.6 10-12 |
6.8 10-10 |
| |
|
|
|
|
|
|
| PP (Poly Propylene) |
CO2 |
0.17 |
1.4 10-11 |
1.4 10-11 |
2.4 10-12 |
4.7 10-9 |
O2 |
0.029 |
2.5 10-11 |
2.5 10-11 |
7.4 10-13 |
1.0 10-9 |
| |
|
|
|
|
|
|
PC (Poly Carbonate) |
CO2 |
5.0 |
9.6 10-13 |
1 10-12 |
5 10-12 |
1 10-8 |
O2 |
0.36 |
4.2 10-12 |
4.2 10-12 |
1.5 10-12 |
2.1 10-9 |
N2 |
0.077 |
2.6 10-12 |
2.6 10-12 |
2.0 10-13 |
2.5 10-10 |
| |
|
|
|
|
|
|
PS (Poly Styrene) |
CO2 |
0.80 |
5.8 10-12 |
5.8 10-12 |
4.6 10-12 |
8.9 10-9 |
O2 |
0.15 |
1.1 10-11 |
1.1 10-11 |
1.7 10-12 |
2.4 10-9 |
N2 |
0.021 |
9.6 10-12 |
9.6 10-12 |
2.0 10-13 |
2.5 10-10 |
| |
|
|
|
|
|
|
PVC (Poly Vinyl Chloride) |
CO2 |
0.47 |
2.5 10-13 |
2.5 10-13 |
1.2 10-13 |
2.4 10-10 |
O2 |
0.029 |
1.2 10-12 |
1.2 10-12 |
3.5 10-14 |
4.9 10-11 |
N2 |
0.023 |
3.8 10-13 |
3.8 10-13 |
8.7 10-15 |
1.1 10-11 |
H2 |
0.026 |
5.0 10-11 |
5.0 10-11 |
1.3 10-12 |
1.2 10-10 |
* D0 is the "zero concentration" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
** D| is the "weighted average" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
|
|
| |
Conditions |
System Temperature: |
25 degrees Celsius |
| System Pressure: |
1 Bar |
| Activity of Permeant |
100% |
| |
Material |
Permeant |
Solubility |
D0* |
D|** |
Permeability |
[-] |
[-] |
m3stp / m3 x bar |
m2/ s |
m2/ s |
[m3stp / m3] x [m2 / s] |
gram / m s |
99 Al |
H2 |
2 10-8 |
1 10-11 |
1 10-11 |
2 10-19 |
2 10-17 |
Fe - 40 Al |
H2 |
5 10-4 |
4 10-13 |
4 10-13 |
2 10-16 |
2 10-14 |
Fe - 25 Al |
H2 |
3 10-3 |
1 10-12 |
1 10-12 |
3 10-15 |
3 10-13 |
| Fe- 18 Al |
H2 |
1 10-1 |
1 10-11 |
1 10-11 |
1 10-12 |
9 10-11 |
99 Fe |
H2 |
2 10-1 |
6 10-9 |
6 10-9 |
1 10-9 |
9 10-8 |
Stainless Steel (304) |
H2 |
2 10-1 |
5 10-10 |
5 10-10 |
1 10-10 |
9 10-9 |
High Strength
Steel
(X - 52)
|
H2 |
8 10-2 |
3 10-13 |
3 10-13 |
2 10-14 |
2 10-12 |
High Strength
Steel
(X - 65) |
H2 |
1 10-2 |
3 10-13 |
3 10-13 |
3 10-15 |
2 10-13 |
* D0 is the "zero concentration" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
** D| is the "weighted average" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
|
|
| |
Process Conditions |
System Temperature: |
37 degrees Celsius |
| System Pressure: |
1 Bar |
| Activity of Permeant: |
100% |
| |
Polymer |
Permeant
(liquid) |
Solubility
(liquid) |
D0* |
|
Permeability
|
[-] |
[-] |
m3 / m3 |
m2 / s |
m2 / s |
[m3 / m3] x [m2/s] |
gram / m s |
Thermosets |
|
Unsaturated Polyester Resin
100% amorphous
|
Water |
0.011 |
4 10-12 |
4 10-12 |
4 10-14 |
4 10-8 |
Methanol |
0.12 |
1 10-13 |
6 10-13 |
8 10-14 |
6 10-8 |
Toluene |
0.21 |
3 10-15 |
1 10-13 |
2 10-14 |
2 10-8 |
Gasoline |
0.17 |
5 10-15 |
8 10-14 |
1 10-14 |
1 10-8 |
| |
|
|
|
|
|
|
Novolac Vinyl
Ester Resin
100% amorphous
|
Water |
0.013 |
1 10-12 |
1 10-12 |
1 10-14 |
1 10-8 |
Methanol |
0.16 |
4 10-14 |
5 10-13 |
8 10-14 |
6 10-8 |
Toluene |
0.12 |
1 10-15 |
6 10-15 |
7 10-16 |
6 10-10 |
Gasoline |
0.10 |
2 10-15 |
9 10-15 |
9 10-16 |
7 10-10 |
| |
|
|
|
|
|
|
Bisphenol-A
Epoxy Resin
100% amorphous
|
Water |
0.015 |
9 10-13 |
9 10-13 |
1 10-14 |
1 10-8 |
Methanol |
0.16 |
2 10-14 |
3 10-13 |
5 10-14 |
4 10-8 |
Toluene |
0.15 |
1 10-15 |
5 10-15 |
8 10-16 |
7 10-10 |
Gasoline |
0.05 |
1 10-15 |
2 10-15 |
1 10-16 |
9 10-11 |
Thermoplast |
|
HDPE
77% crystalline
|
Water |
0.0002 |
1 10-11 |
1 10-11 |
2 10-15 |
2 10-9 |
Benzene |
0.10 |
7 10-13 |
9 10-12 |
1 10-12 |
9 10-7 |
Toluene |
0.11 |
6 10-13 |
1 10-11 |
1 10-12 |
1 10-6 |
Styrene |
0.10 |
4 10-13 |
5 10-12 |
6 10-13 |
5 10-7 |
Gasoline |
0.09 |
6 10-13 |
6 10-12 |
5 10-13 |
4 10-7 |
| |
|
|
|
|
|
|
* D0 is the "zero concentration" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
** D| is the "weighted average" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws. |
|
Process Conditions |
System Temperature: |
37 degrees Celsius |
| System Pressure: |
1 Bar |
| Activity of Permeant: |
40% and 90% |
| |
Polymer |
Permeant, Activity
|
Solubility
(vapour) |
D0* |
D|** |
Permeability
|
[-] |
[-],[%] |
m3stp /
m3 x bar |
m2 / s |
m2 / s |
[m3stp / m3] x [m2 / s] |
gram
/ m s |
Thermosets |
|
Unsaturated Polyester Resin
|
Water, 40% |
2 102 |
4 10-12 |
4 10-12 |
1 10-11 |
1 10-8 |
Water, 90% |
2 102 |
4 10-12 |
4 10-12 |
5 10-11 |
4 10-8 |
| |
|
|
|
|
|
|
Novolac Vinyl Ester Resin
|
Water, 40% |
3 102 |
1 10-12 |
1 10-12 |
5 10-12 |
4 10-9 |
Water, 90% |
3 102 |
1 10-12 |
1 10-12 |
2 10-11 |
1 10-8 |
| |
|
|
|
|
|
|
Bisphenol-A Epoxy Resin
|
Water, 40% |
3 102 |
9 10-13 |
9 10-13 |
4 10-12 |
3 10-9 |
Water, 90% |
3 102 |
9 10-13 |
9 10-13 |
2 10-11 |
1 10-8 |
Thermoplasts |
|
High Density Polyethylene
|
Water, 40% |
4 |
1 10-11 |
1 10-11 |
6 10-13 |
5 10-10 |
Water, 90% |
4 |
1 10-11 |
1 10-11 |
2 10-12 |
2 10-9 |
| |
|
|
|
|
|
|
Polyamide 6 |
Water, 40% |
1.1 103 |
5 10-15 |
1 10-13 |
3 10-12 |
2 10-9 |
Water, 90% |
2.8 103 |
5 10-15 |
3 10-13 |
5 10-11 |
4 10-8 |
| |
|
|
|
|
|
|
Polycarbonate |
Water, 40% |
3 101 |
8 10-14 |
1 10-13 |
1 10-13 |
2 10-10 |
Water, 90% |
9 101 |
8 10-14 |
|
1 10-12 |
1 10-9 |
| * D0 is the "zero concentration" mutual diffusion coefficient interpreted using Fick's 1st & 2nd Laws.
** D| is the "weighted average" mutual diffusion coefficient interpreted using Fick's 1st & 2nd Laws. |
|
Process Conditions |
System Temperature: |
37 degrees Celsius |
| System Pressure: |
1 Bar |
| Activity of Permeant: |
100% |
| |
Polymer |
Permeant
|
Solubility
|
Swelling |
Diffusion*
|
Permeability |
Retention** |
[-] |
[-] |
[vol %] |
[vol %] |
[m2 / s] |
[gram / m s] |
[%] |
Perform. Polymer + Carb. Fibre (CF) |
|
|
|
|
|
|
PPS + 65 wt% CF |
Water |
0.06 |
0 |
3 10-12 |
2 10-9 |
96 |
PEEK + 65 wt% CF |
Water |
0.2 |
0 |
1 10-13 |
2 10-10 |
95 |
LQP + 65 wt% CF |
Water |
|
|
|
|
|
EPXY + 65 wt% CF |
Water |
|
|
|
|
|
PA + 65 wt% CF |
Water |
|
|
|
|
|
Cast Thermosets |
|
Unsaturated
Polyester
Resin
|
Water |
1.1 |
~0 |
4 10-12 |
4 10-8 |
90 |
Methanol |
12 |
8 |
6 10-13 |
6 10-8 |
81 |
Toluene |
21 |
18 |
1 10-13 |
2 10-8 |
70 |
Gasoline |
17 |
14 |
8 10-14 |
1 10-8 |
74 |
| |
|
|
|
|
|
|
Novolac Vinyl
Ester Resin
|
Water |
1.3 |
~0 |
1 10-12 |
1 10-8 |
95 |
Methanol |
16 |
13 |
5 10-13 |
6 10-8 |
80 |
Toluene |
12 |
10 |
6 10-15 |
6 10-10 |
83 |
Gasoline |
10 |
8 |
9 10-15 |
7 10-10 |
86 |
| |
|
|
|
|
|
|
Bisphenol-A
Epoxy Resin
|
Water |
1.5 |
~0 |
9 10-13 |
1 10-8 |
97 |
Methanol |
16 |
13 |
3 10-13 |
4 10-8 |
82 |
Toluene |
15 |
13 |
5 10-15 |
7 10-10 |
75 |
Gasoline |
5 |
3 |
2 10-15 |
9 10-11 |
92 |
Cast Thermoplast |
|
HDPE
|
Water |
0.02 |
0 |
1 10-11 |
2 10-9 |
99 |
Benzene |
10 |
~1 |
9 10-12 |
9 10-7 |
92 |
Toluene |
11 |
2 |
1 10-11 |
1 10-6 |
89 |
Styrene |
10 |
1 |
5 10-12 |
5 10-7 |
91 |
Gasoline |
9 |
~0 |
6 10-12 |
4 10-7 |
93 |
| |
|
|
|
|
|
|
* The diffusion coefficient is the "weighted average" mutual diffusion coefficient interpreted on basis of Fick's 1st & 2nd Laws.
** E modulus strength retention after 6 months of exposure [sample thickness 400 micrometer].
For materials that show slow chemical degradation the retention does not become stationary.
Please contact us for more information. |
|
| Solubility Parameters |
| Conditions & Legend |
Temperature: 25 degrees Celsius |
δt = total parameter
δd = dispersion component
δp = polar component
δh = H-bond component |
| |
Pressure: 1 Bar |
| |
| Polymer |
δ (MPA0.5) |
δd (MPA0.5) |
δp (MPA0.5) |
δh (MPA0.5) |
| Poly Tetra Fluor Ethylene (PTFE) |
16.7 |
16.2 |
1.8 |
3.4 |
| Poly Propylene (PP) |
18.0 |
18.0 |
0.0 |
1.0 |
| Poly Ethylene (PE) |
18.1 |
18.0 |
0.0 |
2.0 |
| Poly Ethylene Terephthalate (PET) |
20.0 |
18.0 |
6.2 |
6.2 |
| Poly Vinyl Acetate (PVAC) |
20.5 |
15.2 |
11.5 |
7.6 |
| Poly Vinyl Chloride (PVC) |
21.4 |
18.2 |
7.5 |
8.3 |
| Poly Styrene (PS) |
22.7 |
18.6 |
10.5 |
7.5 |
| Epoxy Resin* |
26.3 |
20.4 |
12.0 |
11.5 |
| Poly Vinyl Alcohol (EVOH) |
29.3 |
17.8 |
6.6 |
22.3 |
| Poly Amide (PA 66) |
30.9 |
16.0 |
11.0 |
24.0 |
| Poly Imide |
38.9 |
28.8 |
20.0 |
16.8 |
|
|
| Permeant (GAS) |
δ (MPA0.5) |
δd (MPA0.5) |
δp (MPA0.5) |
δh (MPA0.5) |
| Helium |
3.3 |
3.3 |
0.0 |
0.0 |
| Hydrogen |
7.8 |
7.8 |
0.0 |
0.0 |
| Nitrogen |
5.1 |
5.1 |
0.0 |
0.0 |
| Methane |
9.2 |
9.2 |
0.0 |
0.0 |
| Carbon Dioxide |
15.1 |
11.2 |
7.2 |
7.2 |
|
|
| Permeant (LIQUID) |
δ (MPA0.5) |
δd (MPA0.5) |
δp (MPA0.5) |
δh (MPA0.5) |
| n-Butane |
14.1 |
14.1 |
0.0 |
0.0 |
| n-Pentane |
14.5 |
14.5 |
0.0 |
0.0 |
| Toluene |
18.2 |
18.0 |
1.4 |
2.0 |
| Benzene |
18.6 |
18.4 |
0.0 |
2.0 |
| Styrene |
19.0 |
18.6 |
1.0 |
1.4 |
| Acetone |
20.0 |
15.5 |
10.4 |
7.0 |
| Ethanol |
26.5 |
15.8 |
8.8 |
19.4 |
| Methanol |
29.6 |
15.1 |
12.3 |
22.3 |
| Ethylene Glycerol |
32.9 |
17.0 |
11.0 |
26.0 |
| Glycerol |
36.1 |
17.4 |
12.1 |
29.3 |
| Water |
47.8 |
15.6 |
16.0 |
42.3 |
| |
* Composed of Epichlorohydrin, Bisphenol-A and crosslinked by Aliphatic Amines.
Reference: J.H. Hildebrand, J.M. Prausnitz and R.L. Scott. Regular and Related Solutions.
Van Nostrand-Reinhold, Princeton, 1970. |
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