Membrane Gas Separation



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206. Membrane Gas Separation

9.3.4
Permeation Data 
The main permeation data are collected in Tables 9.1 , 9.2 and Figure 9.10 . The data 
presented are the mean values of six measurements with standard deviations.
Results 6 and 9 from Table 9.2 were obtained by using a newly designed permeation 
cell with strong magnets on both sides of a membrane. The percentage of air enrichment 
was directly measured, while the value of B in this case was just estimated. Values of 
calculated oxygen content in the permeate originate from theoretical consideration [24] . 
We can see that theoretical expectations are in really good agreement with experimental 
data. But, if we present the measured oxygen content in the permeate as a function of the 
magnetic induction (Figure 9.11 ) we can see the tendency of deviation from the linear 
relationship.
All that might be due to the infl uence of a strong magnetic fi eld in which nitrogen and 
oxygen form aggregates [36] which carry more nitrogen, and spoil, in a sense, the separa-
tion process.
-16
-14
-12
-10
-8
-6
-4
-2
0
0
1
2
3
4
5
6
7
t
ln[Q-Qs]
ln[2lc
0
/
Π
2
]
Figure 9.9 An example of late - time permeation curve according to Equation (9.23). 
Reprinted with permission from Journal of Membrane Science, On the air enrichment by 
polymer magnetic membranes by A. Rybak, Z. J. Grzywna and W. Kaszuwara, 336, 1 – 2, 
79 – 85, Copyright (2009) Elsevier Ltd


Air Enrichment by Polymeric Magnetic Membranes
171
Table 9.1  Mass transport coeffi cients for various membranes 
No. Membrane
B (mT) N 
2
, pure

2
, in air
P
×
10 
7
La(l)
 
Δ
 c
0
P
×
10 
7
La(l)
 
Δ
 c
0
cm
cm
cm s cmHg
STP
2
3
(
) (
)
(s)
cm
cm
STP
3
3
(
)
cm
cm
cm s cmHg
STP
2
3
(
) (
)
(s)
cm
cm
STP
3
3
(
)
1
Flat EC
0.00
0.19
±
0.01
1.37
±
0.10 0.71
±
0.05
0.19
±
0.01
1.21
±
0.01 0.50
±
0.04
2
EC + 1.30 g 
of Nd
0.00
0.22
±
0.01
1.23
±
0.10 0.73
±
0.07
0.22
±
0.01
1.31
±
0.01 0.39
±
0.04
3
EC + 1.23 g 
of Nd
0.50
0.31
±
0.01
0.52
±
0.04 0.71
±
0.05
0.46
±
0.01
0.47
±
0.01 0.37
±
0.03
4
EC + 1.38 g 
of Nd
0.79
0.34
±
0.01
1.03
±
0.10 0.73
±
0.07
0.94
±
0.01
0.35
±
0.01 0.37
±
0.03
5
EC + 1.49 g 
of Nd
1.25
0.42
±
0.02
0.83
±
0.07 0.72
±
0.07
1.98
±
0.02
0.30
±
0.01 0.39
±
0.04
No
Membrane
B (mT) O 
2
, pure

2
, in air

.
10 
7
La(l)
 
Δ
  c 
0

.
10 
7
La(l)
 
Δ
  c 
0
cm
cm
cm s cmHg
STP
2
3
(
) (
)
(s)
cm
cm
STP
3
3
(
)
cm
cm
cm s cmHg
STP
2
3
(
) (
)
(s)
cm
cm
STP
3
3
(
)
1
Flat EC
0.00
0.23
±
0.01
1.21
±
0.10 0.63
±
0.05
0.22
±
0.01
1.17
±
0.01 0.11
±
0.01
2
EC + 1.30 g 
of Nd
0.00
0.24
±
0.01
1.35
±
0.10 0.60
±
0.05
0.22
±
0.01
1.26
±
0.01 0.12
±
0.01
3
EC + 1.23 g 
of Nd
0.50
0.52
±
0.01
0.51
±
0.05 0.62
±
0.05
0.77
±
0.01
0.45
±
0.01 0.11
±
0.01
4
EC + 1.38 g 
of Nd
0.79
0.63
±
0.01
0.56
±
0.06 0.63
±
0.05
2.23
±
0.01
0.32
±
0.01 0.11
±
0.01
5
EC + 1.49 g 
of Nd
1.25
1.18
±
0.02
0.52
±
0.05 0.64
±
0.05
5.79
±
0.01
0.23
±
0.01 0.12
±
0.01
Source: Reprinted with permission from Journal of Membrane Science, On the air enrichment by polymer magnetic membranes by A. Rybak, Z. J. Grzywna and W. Kaszuwara, 
336, 1 – 2, 79 – 85 Copyright (2009) Elsevier Ltd 
*  
Δ
 c
0
was obtained using a late time permeation curve according to Equation (9.23) . Other methods mentioned above could be used only in the case of the suffi cient amount of 
data, and for an ‘ ideal Fickian ’ description of a permeation process.


172
Membrane Gas Separation
0
0,000
t(s)
0,002
Q
a
(l, t)
0,004
La=1,17 s
La=0,45 s
La=0,32 s
La=0,23 s
Figure 9.10 Downstream absorption permeation curves for various polymer and 
magnetic membranes. Points marked as: squares, magnetic membrane with B = 1.25 mT; 
stars, magnetic membrane with B = 0.79 mT; triangles, magnetic membrane with 
 B = 0.50 mT; asterisk, plane EC membrane
Table 9.2  Comparison of measured and calculated air enrichment data for various 
membranes 
No
Membrane
B (mT)
Measured oxygen 
content in permeate (%)
Predicted (calculated) oxygen 
content in permeate (%)
1
EC
0.00
23.8
±
1.0
25.0
2
EC 
0.0
0.00
22.1
±
1.1
25.0
3
EC 
0.50
0.50
30.7
±
1.1
33.3
4
EC 
0.79
0.79
40.7
±
1.1
38.2
5
EC 
1.25
1.25
43.8
±
1.1
45.8
6
EC 
2.25
2.25
55.6
±
1.4
62.5
7
PPO
0.00
37.4
±
1.2

8
PPO 
1.70
1.70
54.1
±
1.4

9
PPO 
2.70
2.70
61.9
±
1.5

9.4
Results and Discussion 
We have found (Table 9.3 ) that EC fi lms for pure and mixed components as well as 
EC + Nd/N 
2
form ideal Fickian systems, while EC + Nd/N 
2
air, EC + Nd/O 
2
and EC + Nd/

2
air, do not. Based on that we can calculate  D
¯  and  
Δ
 c
0
from the appropriate ‘ ideal ’
permeation curve to get a sort of a reference point for non - ideal cases.
We can separate the drift and diffusion in an overall fl ux assuming that the diffusional 
contribution to the overall fl ux is magnetic fi eld independent.


Air Enrichment by Polymeric Magnetic Membranes
173
l
D
J
Bi
=

w
Bi
Δ
c
0
Δ
c
0
plane EC
drift 
(9.24)
J
J
w
c
Bi
Bi
=
+
0
0
Δ
(9.25)
Here ‘ B 
i
’ stands for magnetic induction of a membrane. The drift coeffi cient can be cal-
culated for an imposed induction B from equation:
w
J
J
c
Bi
Bi
=

0
0
Δ
(9.26)
and its values for different values of B are collected in Table 9.4 .
As can be seen from Table 9.5 (pure gases) the infl uence of drift is meaningful only 
for oxygen, whose transport is strongly affected by the magnetic fi eld.
Quite a different situation happens for air transport through magnetic membranes (i.e. 
with a nonzero induction), where much larger differences between the nitrogen and 
oxygen diffusion coeffi cients were observed (Table 9.6 ). Surprisingly, it was found that 
not only is oxygen transport affected by the magnetic fi eld, but the nitrogen diffusion is 
as well.
0
10
20
30
40
50
60
70
2,5
2
1,5
1
0,5
0
B [mT]
oxygen content in permeate [%]
Figure 9.11 Dependence of the oxygen content in permeate vs. magnetic fi eld induction. 
Points marked as rhombus were obtained in experiment, points marked as squares were 
predicted by the theory


174
Membrane Gas Separation
Table 9.3  Diffusion coeffi cients for ideal, and non - ideal, Fickian systems 
Membrane
Ideal Fickian system

2
pure

2
pure

2
in air

2
in air
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)
Flat EC
0.8
±
0.2
0.8
±
0.2
1.1
±
0.2
0.9
±
0.1
1.1
±
0.2
1.1
±
0.1
1.0
±
0.1
1.1
±
0.2
1.0
±
0.1
1.2
±
0.1
0.9
±
0.2
0.9
±
0.2
1.1
±
0.4
0.9
±
0.1
1.1
±
0.2
0.9
±
0.1
0.9
±
0.1
1.4
±
0.2
1.0
±
0.1
1.2
±
0.1
EC + 1.30 g 
Nd
1.3
±
0.2
1.1
±
0.2
1.4
±
0.3
1.3
±
0.2
0.9
±
0.2
out of the case
out of the case
out of the case
EC + 1.38 g 
Nd
1.4
±
0.3
1.0
±
0.2
1.3
±
0.3
1.1
±
0.2
0.9
±
0.2
out of the case
out of the case
out of the case
Membrane
Non - ideal Fickian system

2
pure

2
pure

2
in air

2
in air
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
 D
¯
 

L
 

3
 

4
 

5
 
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)
10 
5
(cm 
2
/s)

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