HUNGARIAN JOURNAL
OF 
INDUSTRY AND CHEMISTRY 

Vol. pp.45(1) pp. 5–8 (2017) 

hjic.mk.uni-pannon.hu 

DOI: 10.1515/hjic-2017-0002 

SEPARATION OF GASES BY MEMBRANES:  
THE EFFECTS OF POLLUTANTS ON THE STABILITY OF MEMBRANES 

NÁNDOR NEMESTÓTHY* 

Research Institute of Bioengineering, Membrane Technology and Energetics, University of 
Pannonia, Egyetem u. 10, Veszprém, H-8200, HUNGARY 

The long-term stability of membranes is determined mainly by their sensitivity to pollutants. Their stability was 
tested using a novel, multichannel measuring system, which is based on pressure differences. This measuring 
system is suitable to determine the changes in permeability of polymer membranes. The damaging effects of 
H2S, BTX and n-dodecane were investigated in terms of polyimide gas separation membranes using nitrogen 
gas. 

Keywords: multichannel test equipment, pressure difference, hydrogen sulphide, BTX 

1. Introduction 

Previously, it was thought that the stability of memb-
ranes is determined by the mechanical stress (shear) and 
the natural aging of polymers. Recently, however, it has 
been confirmed that their stability is limited mainly by 
the sensitivity of membranes to certain pollutants. These 
aggressive compounds, pollutants, e.g. chlorine, 
hydrogen sulphide, hydrocarbons, etc., may damage the 
structure of the polymer, thus its physical and chemical 
properties change, and consequently the permselectivity 
of the membrane changes, as well. 

It is known that polymeric reverse osmosis memb-
ranes are sensitive to strong oxidising agents, especially 
chlorine compounds [1], therefore, intensive research 
has been conducted to avoid or at least reduce any 
damage [2-3]. Similar levels of membrane degradation 
are observed in proton-exchange membrane (PEM) fuel 
cells and batteries containing membranes, where oxi-
dising compounds are in contact with the membranes, as 
well [4-5]. 

The stability of polymeric gas separation memb-
ranes has hardly been investigated. The long-term eff-
ects of H2S on inorganic membranes has been studied 
by Australian researchers at low concentrations (50 
ppm) [6]. However, H2S may not only cause long-term, 
but immediate damage, mainly in the form of swelling, 
which strongly influences the gas transport properties of 
membranes. Koros and co-workers presented the effects 
of extremely high H2S concentrations on a polymer 
membrane (50,000 - 100,000 ppm) [7]. 

In the field of membrane technology, sensitivity 
can be measured by a sort of effectiveness unit. The 

                                                           
*Correspondence: nemesn@almos.uni-pannon.hu 

product of the concentration and time period yields a 
value where the effectiveness of the membrane decr-
eases from 95 to 90 and then to 70% of its original 
value (e.g. 1000 ppm*hour means that the membrane 
was exposed to 1000 ppm of pollutant for 1 hour, or 0.1 
ppm of pollutant for 10,000 hours during the tests). 

According to the literature these types of 
measurements have yet to be published for gas 
separation membranes, thus the aim of this work was to 
design, construct and operate a piece of test equipment 
that conducts reliable laboratory tests. 

For the determination of stability, direct and 
indirect methods can be used to measure the gas 
volumes passing through the membranes. Direct 
methods are usually preferred, and – if the composition 
of the gas is known – are more exact than indirect ones. 
However, when the gas composition varies and small 
amounts of gases need to be measured, indirect methods 
are often more suitable. In this work an indirect method 
based on a pressure differential technique was chosen, 
where the pressure of a closed vessel is measured and 
the varying pressure yields information about the 
volume of the gas passing through the membrane.  

During the investigation the effects of pollutants 
on the permeability of nitrogen was to be studied. The 
following pollutants were used: 

 
 compounds containing sulphur at associated 

gas  
 BTX mixture (benzene, toluene, xylene)  
 heavy hydrocarbons  
 
In this research the aim was to determine 

quantitatively the effects of pollutants on the 
membranes to define the tolerance range of particular 
membranes. 

 
 



  NEMESTÓTHY 

Hungarian Journal of Industry and Chemistry 

6

 
Figure 1. The small modules constructed for the tests 

2. Experimental 

For this series of measurements, polyimide gas 
separation membranes (synthesised by UBE) were used. 
They were taken from a hollow fibre module and can 
accurately model the properties of industrial gas 
separation membranes. From the hollow fibres small 
modules containing 6 capillaries were constructed 
(Fig.1) and their ends were closed, thus their tests were 
carried out in a “sack” configuration. 

In the design of the test system it was important 
that several parallel measurements should be conducted 
and the measuring channels combined with each other. 
The scheme of a measuring channel can be seen in Fig.2  

The gas was introduced into the measuring system 
through valve V1 (which can be adjusted by valve V2 if 
necessary). Before measurements were taken the 
pressure of the vessel was checked by pressure 
transducer PT1. To start the test the pressure was 
adjusted by regulating valve PV1, which was checked 
by pressure transducer PT2. Then the membrane was 
installed into the thermostatic system in a way that 
ensured its mobility was not restricted, thus the 
permeation of gas could not influence the flux.  

A photograph of the measuring system is shown in 
Fig.3.  For the permeability measurements nitrogen gas 
from a cylinder was used (99.5%; Messer Hungarogáz 
Kft., Hungary). 

The permeability of the membrane was determined 
from the pressure of the vessel and the transmembrane 
pressure measured on-line during the experiments. In 
the experiments, H2S, methyl mercaptan and ammonia 
(compounds containing S or N), oleic acid, ethyl 
 

 

Figure 2. The scheme of the test system 

 
 
Figure 3. The test system  

 
alcohol, moreover, a benzene-toluene-xylene mixture 
(BTX) and n-dodecane (as a heavier hydrocarbon) were 
used as pollutants. 

For the stability experiments the small membrane 
modules were put in a closed vessel (Fig.4) where the 
headspace was saturated with the given pollutant. The 
vessels were placed in a thermostatic incubator at 27 °C 
usually for between 1 and 7 days. 

Certain materials (e.g. BTX) damaged the epoxy 
resin glue used to adhere the fibres of the membranes, 
therefore, these experiments were repeated using poly-
ether-sulfone glue instead. 

3. Results  

The nitrogen permeability of the membranes was 
determined before and after the incubations.  

In the preliminary experiments, the ammonia 
solution and methyl mercaptan severely damaged the 
surface of the membranes, thus no flux could be 
measured. Oleic acid and ethyl alcohol hardly 
influenced the flux, while BTX, H2S and n-dodecane 
changed the permeability of nitrogen considerably. 

For further investigation of the pollutants an 
experimental design was constructed, using appropriate 

 

 
Figure 4: The membranes in the closed vessel 

 



THE EFFECTS OF POLLUTANTS ON THE STABILITY OF MEMBRANES 

45(1) pp. 5–8 (2017) 

7

Table 1. The parameters of the experimental design  
 

pollu-
tant 

cmin 
ppm 

cav 
ppm 

cmax 
ppm 

tmin  
d 

tav 
d 

tmax  
d 

H2S 100,000 300,000 500,000 1  3.5  7  
BTX 
mixt. 

1,000 750 500 1  3.5  7  

dode-
cane 

1,000 5,500 10,000 1  3.5  7  

 
statistical methods. The parameters selected were the 
concentrations of the pollutants (minimum, maximum 
and average) and the incubation time (minimum, 
maximum and average). The Statistica 8 computer 
program was applied to the design presented in Table 1.  

Firstly the effect of H2S on the nitrogen 
permeability of the membranes was measured. The 
experimental results are presented in Fig.5. 

It can be seen that the permeability of nitrogen 
increased even when the concentrations of pollutants 
were low and rose by using higher concentrations and 
longer periods of exposure.  

From the H2S concentration and the incubation time 
it was possible to calculate a special parameter of 
exposure with the unit of ppm*h. Permeability was 
presented as a function of this parameter (Fig.6), where 
an almost linear relationship was observed. 

The results suggest that the process can be described 
as a first-order reaction, which means that no safe limit 
can be determined where H2S is regarded as harmless, 
on the contrary, it should be considered at all times.  

The effect of the BTX mixture was studied using a 
similar methodology. The results are summarized in 
Fig.7. This figure shows that the permeability of 
nitrogen increased at low concentrations of the BTX 
mixture. At higher concentrations and over longer 
periods of time, no further significant changes were 
observed. 

The exposure parameter was also calculated in the 
unit of ppm*h and permeability was presented as its 
function (Fig.8). The diagram can be described as a 
saturation-type curve. 

 
 

2**(2-0) design; MS Residual=49886.27

 > 2000 
 < 2000 
 < 1500 
 < 1000 
 < 500 
 < 0 

 
Figure 5. The effect of H2S on the nitrogen 
permeability 

Exposure [M ppm * h]

0 20 40 60 80 100

P
e
rm

e
a
b
il
it
y
 c

h
a
n
g
e
 [
%

]

0

500

1000

1500

2000

2500

Figure 6. Permeability changes against exposure to H2S 
 
 

2**(2-0) design; MS Residual=2675.592

 > 400 
 < 360 
 < 310 
 < 260 
 < 210 
 < 160 
 < 110 
 < 60 

Figure 7: The effect of the BTX mixture  

 
In the last series of experiments, the effect of 

exposure to n-dodecane was investigated experi-
mentally. The results are presented in Fig.9. 

n-dodecane caused – unlike H2S and BTX – a 
reduction in the permeability of nitrogen even at low 
concentrations. The flux fell to zero at higher 
concentrations and over longer incubation periods. 

Permeability was investigated as a function of 
exposure (Fig.10). The process can be described as a 
first-order reaction, thus the effect of heavier 
hydrocarbons, e.g. n-dodecane, should always be 
considered. 

Exposure [k ppm * h]

0 20 40 60 80 100 120 140 160 180

p
e

rm
e

a
b

ili
ty

 c
h

a
n

g
e

 [
%

]

0

100

200

300

400

 
Figure 8: Permeability changes against BTX exposure 



  NEMESTÓTHY 

Hungarian Journal of Industry and Chemistry 

8

2**(2-0) design; MS Residual=40.32141

 > 100 
 < 96 
 < 76 
 < 56 
 < 36 

 
Figure 9: The effect of n-dodecane  

4. Conclusion  

The long-term stability of polyimide gas separation 
membranes was tested against various pollutants: H2S, a 
BTX mixture and n-dodecane. These compounds 
significantly affected the nitrogen permeability of the 
membranes which were described by using a special 
parameter of exposure. It was found that H2S and the 
BTX mixture increased the permeability, while n-
dodecane reduced the permeability of the membranes. 
Further investigations are planned to investigate the 
effect of other pollutants, moreover, to determine the 
permeability of additional gases, e.g. carbon dioxide, 
methane, etc. 

Acknowledgement  

We acknowledge the financial support of Széchenyi 
2020 under the EFOP-3.6.1-16-2016-00015 project. 
This research was supported by the János Bolyai 
Research Scholarship of the Hungarian Academy of 
Sciences.  

REFERENCES  

[1] Glater, J.; Hong, S.K.; Elimelech, M.: The search 
for a chlorine-resistant reverse osmosis membrane, 
Desalination, 1994 95(3), 325-345 DOI: 
10.1016/0011-9164(94)00068-9 

Exposure [ k ppm * h]

0 50 100 150 200

p
e

rm
e

a
b

ili
ty

 c
h
a

n
g

e
 [

%
]

0

10

20

30

40

50

60

70

 
Figure 10. Change in permeability against exposure to 
n-dodecane 

 
 

[2] Zhang, Y.; Zhao, C.; Yan, H.; Pan, G.; Guo, M.; 
Na, H.; Liu, Y.: Highly chlorine-resistant 
multilayer reverse osmosis membranes based on 
sulfonated poly(arylene ether sulfone) and 
poly(vinyl alcohol), Desalination, 2014 336, 58-63 
DOI: 10.1016/j.desal.2013.12.034 

[3] Gohil, J.M.; Suresh, A.K.: Chlorine attack on 
reverse osmosis membranes: Mechanisms and 
mitigation strategies, J. Membr. Sci., 2017 541, 
108-126 DOI: 10.1016/j.memsci.2017.06.092 

[4] Huang, X.; Pu, Y.; Zhou, Y.; Zhang, Y.; Zhang, 
H.: In-situ and ex-situ degradation of sulfonated 
polyimide membrane for vanadium redox flow 
battery application, J. Membr. Sci., 2017 526, 281-
292 DOI: 10.1016/j.memsci.2016.09.053 

[5] Lapicque, F.; Belhadj, M.; Bonnet, C.; Pauchet, J.; 
Thomas, Y.: A critical review on gas diffusion 
micro and macroporous layers degradations for 
improved membrane fuel cell durability, J. Power 
Sources, 2016 336, 40-53 DOI: 
10.1016/j.jpowsour.2016.10.037 

[6] Uhlmann, D.; Smart, S.; Diniz da Costa, J.C.: H2S 
stability and separation performance of cobalt 
oxide silica membranes, J. Membr. Sci., 2011 
380(1), 48-54 DOI: 1016/j.memsci.2011.06.025 

[7] Kraftschik, B.; Koros, W.J.; Johnson, J.R.; Karvan, 
O.: Dense film polyimide membranes for 
aggressive sour gas feed separations, J. Membr. 
Sci., 2013 428, 608-619 DOI: 
10.1016/j.memsci.2012.10.025